Cogeneration systems and methods for generating heating and electricity

ABSTRACT

Systems and methods are disclosed for a cogeneration system for providing heating, cooling, and/or electricity to an enclosure. The system includes a heat engine for heating and supplying electricity to the enclosure through fluid transfer from the heat engine to the enclosure to transfer thermal energy from the fluid to the enclosure. The system further includes a heat pump configured to supply at least heating and cooling to the enclosure through movement of fluid from the heat pump to the enclosure to transfer thermal energy from the fluid to the enclosure.

CROSS REFERENCE TO RELATED APPLICATIONS

This disclosure claims priority to U.S. Provisional App. No. 62/525,513,filed Jun. 27, 2017, entitled “COGENERATION SYSTEM FOR GENERATINGHEATING, COOLING, AND/OR ELECTRICITY,” the entirety of which isincorporated by reference herein. This application is related, but doesnot claim priority, to U.S. Patent Ser. Nos. ______ (IMB0002PA1) and______ (IMB0002PA2) and International PCT Patent application Ser. No.______ (IMB0002WO), each of which were filed on the same date as thepresent application.

FIELD OF THE DISCLOSURE

This disclosure relates to a cogeneration system, and more particularlyto a cogeneration system for generating heating, cooling, and/orelectricity.

BACKGROUND

Many communities today receive electric power from a central powerstation (e.g., a power plant) via a network of a transmission anddistribution lines otherwise known as the grid. Centralized powerstations typically process fuel (e.g., coal, natural gas, nuclear, oil,)to generate thermal energy which drives a heat engine to producemechanical work which is then converted into electricity. These powerstations may include a prime mover, such as a steam or gas turbine, toaccomplish work. Using the thermal energy generated by processing thefuel (e.g., through combustion or chemical reaction) the prime mover canbe operated (e.g., using dynamic gas or vapor pressure) to perform work.The prime mover is commonly coupled to a generator to convert mechanicalwork into electricity. The generator may produce electricity in responseto movement of the prime mover (e.g., rotation of a shaft coupled to theprime mover). This electricity can then be supplied to consumers via thetransmission and distribution lines of the network.

SUMMARY

In an embodiment, a cogeneration system for providing heating, cooling,and electricity to an enclosure may include a heat engine configured forheating and supplying electricity to the enclosure, a heat pumpconfigured for heating and cooling of the enclosure, a first conduitcoupled to the heat engine, a second conduit coupled to the heat pump,and a third conduit coupled to the heat pump, wherein the heat pump maybe configured to supply heating and cooling to the enclosuresimultaneously. The first conduit may be filled with a first heattransfer fluid, and the first conduit may be constructed and arranged totransfer the first heat transfer fluid from the heat engine to theenclosure such that thermal energy is transferred from the first heattransfer fluid to the enclosure to provide heating to the enclosure. Thesecond conduit may be filled with the first heat transfer fluid, and thesecond conduit may be constructed and arranged to transfer the firstheat transfer fluid from the heat pump to the enclosure such thatthermal energy is transferred from the first heat transfer fluid to theenclosure to provide heating to the enclosure. The third conduit may befilled with a second heat transfer fluid, and the third conduit may beconstructed and arranged to transfer the second heat transfer fluid fromthe heat pump to the enclosure such that thermal energy is absorbed bythe second heat transfer fluid from the enclosure to provide cooling tothe enclosure.

The heat engine may further include a heat exchanger, and the firstconduit may be coupled to the heat exchanger to transfer thermal energyfrom the heat engine to the enclosure. The first conduit and the secondconduit may be constructed and arranged to transfer thermal energy viathe first heat transfer fluid to the enclosure to provide space heatingto the enclosure. The cogeneration system may further include a heatingsystem heat exchanger constructed and arranged to be coupled to aheating system associated with the enclosure, and the first conduit andthe second conduit may be fluidly coupled to the heating system heatexchanger such that thermal energy is transferred from the first heattransfer fluid to the heating system heat exchanger to provide heatingto the enclosure. The cogeneration system may be in combination with theheating system associated with the enclosure. The cogeneration systemmay further include a thermal storage system heat exchanger constructedand arranged to be coupled to a thermal storage system associated withthe enclosure, and the first conduit and the second conduit may befluidly coupled to the thermal storage system heat exchanger such thatthermal energy is transferred from the first heat transfer fluid to thethermal storage system heat exchanger. The cogeneration system may be incombination with the thermal storage system. The thermal storage systemmay be a hot water storage tank, and the first conduit and the secondconduit may be fluidly coupled to the thermal storage system heatexchanger to transfer thermal energy from the first heat transfer fluidto the thermal storage system heat exchanger to heat water in the hotwater storage tank. The cogeneration system may further include acooling system heat exchanger, constructed and arranged to be coupled toa cooling system associated with the enclosure, and the third conduitmay be fluidly coupled to said cooling system heat exchanger so that thesecond heat transfer fluid absorbs thermal energy from the enclosure toprovide cooling to the enclosure. The cogeneration system may be incombination with the cooling system associated with the enclosure.

In embodiments, the first heat transfer fluid and the second heattransfer fluid may contain glycol. The heat engine further may include agenerator and the heat pump further may be an electric motor. Thegenerator may be constructed and arranged to selectively provideelectricity to the electric motor of the heat pump. The heat pump may beconstructed and arranged to provide heating and cooling to the enclosurewithout requiring operation of the heat engine. The heat engine may beconstructed and arranged to provide heating and electricity to theenclosure without requiring operation of the heat pump. The heat engineand the heat pump may be constructed and arranged to be operatedsimultaneously so that the heat engine provides heating and electricityto the enclosure and provides electricity to operate the heat pump, andthe heat pump provides heating and cooling to the enclosure.

In another embodiment, a cogeneration system for providing heating andelectricity to an enclosure may include a heat engine configured forheating and supplying electricity to the enclosure, a heat pumpconfigured for heating of the enclosure, a first conduit coupled to theheat engine, and a second conduit coupled to the heat pump and the firstconduit. Said first conduit may be filled with a heat transfer fluid,and the first conduit may be constructed and arranged to transfer theheat transfer fluid from the heat engine to the enclosure such thatthermal energy is transferred from the heat transfer fluid to theenclosure to provide heating to the enclosure. The second conduit may befilled with the heat transfer fluid, and said second conduit may beconstructed and arranged to transfer the heat transfer fluid from theheat pump to the enclosure such that thermal energy is transferred fromthe heat transfer fluid to the enclosure to provide heating to theenclosure. The first conduit and the second conduit may be fluidlycoupled such that the heat transfer fluid in the first conduit is thesame as the heat transfer fluid in the second conduit.

Said first conduit may be coupled to the second conduit in series suchthat either the heat transfer fluid moves from the second conduit intothe first conduit, or the heat transfer fluid moves from the firstconduit into the second conduit. The heat engine may further include aheat exchanger, and the first conduit may be coupled to the heatexchanger to transfer thermal energy from the heat exchanger to theenclosure, and the heat pump further may include a condenser. The secondconduit may be coupled to the condenser to transfer the thermal energyfrom the condenser to the enclosure. In an embodiment, the first conduitis coupled to the second conduit in series such that either the heattransfer fluid moves from the condenser of the heat pump into the heatexchanger of the heat engine, or the heat transfer fluid moves from theheat exchanger of the heat engine into the condenser of the heat pump.In another embodiment, the cogeneration system may further include valvecoupling the first conduit to the second conduit, and the first conduitmay be coupled to the second conduit in parallel such that the heattransfer fluid from the first conduit is selectively mixed by the valvewith the heat transfer fluid from the second conduit. The heat enginemay further include a heat exchanger, and the first conduit may becoupled to the heat exchanger to transfer thermal energy from the heatexchanger to the enclosure, the heat pump may further include acondenser, and the second conduit may be coupled to the condenser totransfer the thermal energy from the condenser to the enclosure, and thefirst conduit may be coupled to the second conduit in parallel such thatthe heat transfer fluid that moves through the condenser of the heatpump is selectively mixed by the valve with the heat transfer fluid thatmoves through the heat exchanger of the heat engine. In embodiments, theheat transfer fluid within the first conduit and the heat transfer fluidwithin the second conduit contains glycol. The cogeneration system mayfurther include a third conduit coupled to the heat pump. The thirdconduit may be filled with the heat transfer fluid, and the thirdconduit may be constructed and arranged to transfer the heat transferfluid from the heat pump to a heat source such that thermal energy isabsorbed from the heat source by the heat transfer fluid to operate theheat pump and thereby provide cooling to the enclosure. The firstconduit and the second conduit may form a separate piping system fromthe third conduit so that the enclosure absorbs thermal energy from theheat transfer fluid in the first and second conduits and the heattransfer fluid in the third conduit absorbs thermal energy from the heatsource. The heat transfer fluid within the third conduit may not bemixed with the heat transfer fluid within the first conduit and thesecond conduit.

In yet another embodiment, a cogeneration system for providing heatingand electricity to an enclosure may include a heat engine configured toproduce heating and electricity for the enclosure, a heat pumpconfigured to produce heating for the enclosure, a heat reservoirconstructed and arranged to transfer thermal energy from an area outsideof the enclosure to the heat pump, a thermal storage system associatedwith the enclosure and including a thermal storage system heatexchanger, a first conduit coupled to the heat engine, and a secondconduit coupled to the heat pump. The first conduit may be filled with afirst heat transfer fluid, and the first conduit may be constructed andarranged to transfer the first heat transfer fluid from the heat engineto the thermal storage system heat exchanger such that thermal energy istransferred from the first heat transfer fluid to the thermal storagesystem. The second conduit may be filled with the first heat transferfluid, and the second conduit may be constructed and arranged totransfer the first heat transfer fluid from the heat pump to the thermalstorage system heat exchanger such that thermal energy is transferredfrom the first heat transfer fluid to the thermal storage system. Thefirst conduit and the second conduit may be fluidly coupled to thethermal storage system heat exchanger such that the first heat transferfluid from the first conduit and the second conduit is transferred tothe thermal storage system heat exchanger to store thermal energy withinthe thermal storage system.

The thermal storage system may be a hot water storage tank, and thefirst conduit and the second conduit may be fluidly coupled to thethermal storage system heat exchanger to transfer the first heattransfer fluid from the first conduit and the second conduit to thethermal storage system heat exchanger to transfer thermal energy fromthe first heat transfer fluid to a fluid within the hot water storagetank. The cogeneration system may further include a heating system heatexchanger constructed and arranged to be coupled to a heating systemassociated with the enclosure, and the first conduit and the secondconduit may be fluidly coupled to the heating system heat exchanger totransfer the first heat transfer fluid from the first conduit and thesecond conduit to the heating system heat exchanger to provide heatingto the enclosure. The cogeneration system may further include a thirdconduit coupled to the heat pump, the third conduit filled with a secondheat transfer fluid, and the third conduit constructed and arranged totransfer the second heat transfer fluid from the heat pump to a heatsource at which thermal energy is absorbed from the heat source by thesecond heat transfer fluid. The first conduit and the second conduit maybe fluidly coupled to the thermal storage system heat exchanger suchthat the first heat transfer fluid is transferred from the first conduitand the second conduit to the thermal storage system heat exchanger tostore thermal energy within the thermal storage system, and the thirdconduit is fluidly coupled to a cooling system heat exchanger totransfer the second heat transfer fluid from the cooling system heatexchanger to the heat pump to cool the enclosure.

In one other embodiment, a cogeneration system for providing heating,cooling and electricity to an enclosure may include a heat engineconfigured to produce heating and electricity for the enclosure, a heatpump configured to produce heating and cooling for the enclosure, afirst conduit coupled to the heat engine, a second conduit coupled tothe heat pump, a third conduit coupled to the heat pump, and a valvearrangement. The first conduit may be filled with a first heat transferfluid, and the first conduit may be constructed and arranged to transferthe first heat transfer fluid from the heat engine to the enclosure suchthat thermal energy is transferred from the first heat transfer fluid tothe enclosure to provide heating to the enclosure. The second conduitmay be filled with the first heat transfer fluid, and the second conduitmay be constructed and arranged to transfer the first heat transferfluid from the heat pump to the enclosure such that thermal energy istransferred from the first heat transfer fluid to the enclosure toprovide heating to the enclosure. Said third conduit may be filled witha second heat transfer fluid, and the third conduit may be constructedand arranged to transfer the second heat transfer fluid from the heatpump to the enclosure such that thermal energy is absorbed by the secondheat transfer fluid from the enclosure to provide cooling to theenclosure. The valve arrangement may be constructed and arranged toselectively couple the first conduit and the second conduit to transferthe first heat transfer fluid to the enclosure to provide at least oneof space heating and water heating, and to selectively couple the thirdconduit to transfer the second heat transfer fluid to the enclosure toprovide at least one of space cooling and a source of thermal energy forthe heat pump.

The cogeneration system may further include a heating system heatexchanger constructed and arranged to be coupled to a heating systemassociated with the enclosure, and the valve arrangement may beconstructed and arranged to selectively couple the first conduit and thesecond conduit with the heating system to selectively transfer the firstheat transfer fluid to the heating system heat exchanger via the firstconduit and the second conduit. The cogeneration system may furtherinclude a thermal storage system heat exchanger constructed and arrangedto be coupled to a thermal storage system associated with the enclosure,and the valve arrangement may be constructed and arranged to selectivelycouple the third conduit with the thermal storage system to selectivelytransfer the second heat transfer fluid to the thermal storage systemheat exchanger via the third conduit. The cogeneration system may be incombination with the thermal storage system associated with theenclosure. The valve arrangement may be constructed and arranged toselectively couple the third conduit with the thermal storage systemheat exchanger to selectively transfer heat transfer fluid to the heatpump via the third conduit. The cogeneration system may further includea heat reservoir constructed and arranged to be coupled to a thermalstorage system heat exchanger associated with the enclosure, and thevalve arrangement may be constructed and arranged to selectively couplethe third conduit with the thermal storage system heat exchanger toselectively transfer the second heat transfer fluid to the heatreservoir via the third conduit.

In yet one other embodiment, a cogeneration system for providingheating, cooling, and electricity to an enclosure may include a heatengine configured for heating and supplying electricity to theenclosure, a heat pump configured for heating and cooling of theenclosure, a first conduit coupled to the heat engine, a second conduitcoupled to the heat pump, and a third conduit coupled to said heat pump.The heat engine may be configured to supply electricity to operate theheat pump. The first conduit may be filled with a first heat transferfluid, and the first conduit may be constructed and arranged to transferthe first heat transfer fluid from the heat engine to the enclosure suchthat thermal energy is transferred from the first heat transfer fluid tothe enclosure to provide heating to the enclosure. The second conduitmay be filled with the first heat transfer fluid, and the second conduitmay be constructed and arranged to transfer the first heat transferfluid from the heat pump to the enclosure such that thermal energy istransferred from the first heat transfer fluid to the enclosure toprovide heating to the enclosure. Said third conduit may be filled witha second heat transfer fluid, and the third conduit may be constructedand arranged to transfer the second heat transfer fluid from the heatpump to the enclosure such that thermal energy is absorbed by the secondheat transfer fluid from the enclosure to provide cooling to theenclosure.

The cogeneration system may further include a generator constructed andarranged to be coupled to the heat engine, an electrical storage systemconstructed and arranged to be coupled to the generator using one ormore electrical cables, and a power panel constructed and arranged to becoupled to the generator and configured to distribute electricity to theenclosure. The electrical storage system may be configured to receiveelectricity provided by the generator, and to selectively transfer theelectricity to one of the heat pump and the power panel. Thecogeneration system may further include an electrical grid isolationdevice constructed and arranged to decouple the power panel from anelectrical grid meter. The cogeneration system may further include anelectrical grid isolation device constructed and arranged to decouplethe power panel from an electrical grid meter if the enclosure isreceiving power from the generator coupled to the heat engine. Thecogeneration system may further include an electrical grid isolationdevice constructed and arranged to enable electricity produced by thegenerator associated with the heat engine to be transferred to one ormore energy suppliers.

In one another embodiment, a cogeneration system for providing at leastheating to an enclosure may include a heat engine configured for heatingto the enclosure, a heat pump configured for heating the enclosure, afirst conduit coupled to the heat engine, and a second conduit coupledto the heat pump. The cogeneration system may further be for providingelectricity to the enclosure, and the heat engine configured for heatingand supplying electricity to the enclosure. The first conduit may filledwith a first heat transfer fluid constructed and arranged to transferthe first heat transfer fluid from the heat engine to the enclosure suchthat thermal energy is transferred from the first heat transfer fluid tothe enclosure to provide heating to the enclosure. The second conduitmay be filled with the first heat transfer fluid and constructed andarranged to transfer the first heat transfer fluid from the heat pump tothe enclosure such that thermal energy is transferred from the firstheat transfer fluid to the enclosure to provide heating to theenclosure. The first conduit and the second conduit may be fluidlycoupled and configured to at least one of proportion and thermallyisolate the first heat transfer fluid between the first conduit and thesecond conduit.

The heat engine may further include a heat exchanger, and the firstconduit may coupled to the heat exchanger to transfer thermal energyfrom the heat engine to the enclosure. The cogeneration system mayfurther include a heating system heat exchanger constructed and arrangedto be coupled to a heating system associated with the enclosure, and thefirst conduit and the second conduit may be fluidly coupled to theheating system heat exchanger such that thermal energy is transferredfrom the first heat transfer fluid to the heating system heat exchangerto provide space heating to the enclosure. The cogeneration system mayfurther include a thermal storage system heat exchanger constructed andarranged to be coupled to a thermal storage system associated with theenclosure, and the first conduit and the second conduit may be fluidlycoupled to the thermal storage system heat exchanger such that thermalenergy is transferred from the first heat transfer fluid to the thermalstorage system heat exchanger. The thermal storage system may be a hotwater storage tank, and the first conduit and the second conduit may befluidly coupled to the thermal storage system heat exchanger to transferthermal energy from the first heat transfer fluid to the thermal storagesystem heat exchanger to heat water in the hot water storage tank. Thehot water storage tank may include one or more heat exchangers. Thecogeneration system may further include a cooling system heat exchanger,constructed and arranged to be coupled to a cooling system associatedwith the enclosure, a third conduit coupled to the heat pump, the thirdconduit filled with a second heat transfer fluid and constructed andarranged to transfer the second heat transfer fluid from the heat pumpto the enclosure such that thermal energy is absorbed by the second heattransfer fluid from the enclosure to provide cooling to the enclosure.The third conduit may be fluidly coupled to said cooling system heatexchanger so that the second heat transfer fluid absorbs thermal energyfrom the enclosure to provide cooling to the enclosure, and said heatpump may be configured to supply heating and cooling to the enclosuresimultaneously. The first heat transfer fluid and the second heattransfer fluid may contain glycol. The heat engine may further include agenerator, and the heat pump may further an electric motor. Thegenerator may be constructed and arranged to selectively provideelectricity to the electric motor of the heat pump.

The heat pump may be constructed and arranged to provide heating andcooling to the enclosure without requiring operation of the heat engine,the heat engine may be constructed and arranged to provide heating andelectricity to the enclosure without requiring operation of the heatpump, or the heat engine and the heat pump may be constructed andarranged to be operated simultaneously so that the heat engine providesheating and electricity to the enclosure and provides electricity tooperate the heat pump, and the heat pump provides heating and cooling tothe enclosure. The heat engine and the heat pump may be constructed andarranged to be operated simultaneously so that the heat engine providesheating and electricity to one or more portions of the enclosure andprovides electricity to operate the heat pump, and the heat pumpprovides heating and cooling to one or more portions the enclosure.

The cogeneration system may further include a thermal storage systemassociated with the enclosure and comprising one or more heatexchangers, and a heat reservoir. The third conduit may be fluidlycoupled to the thermal storage system and the heat reservoir to move thesecond heat transfer fluid from the one or more heat exchangers of thethermal storage system in a first direction to supply thermal energy tothe heat reservoir to prevent excess ice from accumulating on the heatreservoir, and to move the second heat transfer fluid from the heatreservoir in a second direction opposite the first direction to returnthe second heat transfer fluid to the one or more heat exchangers of thethermal storage system. The cogeneration system may further include avalve arrangement constructed and arranged to selectively couple thefirst conduit and the second conduit to transfer the first heat transferfluid to the enclosure to provide at least one of space heating andwater heating, and to selectively couple the third conduit to transferthe second heat transfer fluid to the enclosure to provide at least oneof space cooling, water cooling, and a source of thermal energy for theheat pump. The cogeneration system may further include a heating systemheat exchanger constructed and arranged to be coupled to a heatingsystem associated with the enclosure, and a thermal storage system heatexchanger constructed and arranged to be coupled to a thermal storagesystem associated with the enclosure. The valve arrangement may beconstructed and arranged to selectively couple the first conduit and thesecond conduit with at least one of the heating system to selectivelytransfer the first heat transfer fluid to the heating system heatexchanger via at least one of the first conduit and the second conduitto provide space heating, and the thermal storage system to selectivelytransfer the first heat transfer fluid to the thermal storage systemheat exchanger via at least one of the first conduit and the secondconduit to provide water heating. The cogeneration system may furtherinclude a cooling system heat exchanger constructed and arranged to becoupled to a cooling system associated with the enclosure. The valvearrangement may be constructed and arranged to selectively couple thethird conduit with at least one of the cooling system to absorb thermalenergy via the cooling system heat exchanger into the second heattransfer fluid in the third conduit to provide space cooling, and thethermal storage system to absorb thermal energy via the thermal storagesystem heat exchanger into the second heat transfer fluid in the thirdconduit to provide at least one of water cooling and the source ofthermal energy for the heat pump.

In embodiments, the cogeneration system(s) as described herein may be incombination a cooling system associated with the enclosure. Thecogeneration system(s) may be in combination with a heating systemassociated with the enclosure. The cogeneration system(s) may be incombination with a thermal storage system associated with the enclosure.The cogeneration system(s) may be in combination with the enclosure. Theenclosure may be a building. The enclosure may be a motor vehicle. Thecogeneration system(s) may be constructed and arranged as an auxiliarypower unit. The auxiliary power unit may be for a motor vehicle. Theauxiliary power unit may be for the enclosure. The heat pump may be avapor compression heat pump. The heat engine may include a fuel burningengine. The heat engine may be a closed-loop Brayton cycle heat engine.

In an embodiment, a method of providing heating, cooling and electricityto an enclosure using a cogeneration system may include generatingthermal energy and electricity by operation of a heat engine, providingthermal energy by operation of a heat pump using the electricity fromthe heat engine, transferring thermal energy from the heat engine andthe heat pump to a first heat transfer fluid, and providing at least oneof space heating and water heating to the enclosure via the first heattransfer fluid at a heating system heat exchanger constructed andarranged to be coupled to a heating system associated with theenclosure. The method may further include providing space cooling to theenclosure by operation of the heat pump via a second heat transfer fluidthat absorbs thermal energy from the enclosure at a cooling system heatexchanger constructed and arranged to be coupled to a cooling systemassociated with the enclosure, wherein at least one of space heating andwater heating are provided to the enclosure simultaneously with spacecooling to the enclosure.

The method may further include providing thermal energy to a thermalstorage system heat exchanger, the thermal storage system heat exchangerconstructed and arranged to be coupled to a thermal storage systemassociated with the enclosure. At least one of space heating and waterheating may be provided to the enclosure before thermal energy isprovided to the thermal storage system heat exchanger. Thermal energymay be provided to the thermal storage system periodically to maintainan amount of thermal energy stored in the thermal storage system above athreshold level. The method may further include providing thermal energyfrom the thermal storage system heat exchanger to the second heattransfer fluid, and providing thermal energy from the second heattransfer fluid to a heat reservoir to prevent excess ice fromaccumulating on the heat reservoir. The method may further includeproviding thermal energy from the thermal storage system heat exchangerto the second heat transfer fluid, and providing thermal energy to theheat pump by absorption of thermal energy from the second heat transferfluid to operate the heat pump. The method may further include providingelectricity to an electrical energy storage system, the electricalenergy storage system constructed and arranged to selectively transferthe electricity to at least one of the heat pump and a power panel.

In yet another embodiment, a method of providing heating, cooling andelectricity to an enclosure using a cogeneration system may includegenerating thermal energy and electricity by operation of a heat engine,providing thermal energy by operation of a heat pump, transferringthermal energy from the heat engine and the heat pump to a first heattransfer fluid, and moving the first heat transfer fluid through a valvearrangement, the valve arrangement constructed and arranged todistribute the first heat transfer fluid to one or more cogenerationsystem components. The method may further include providing at least oneof space heating and water heating to the enclosure via the first heattransfer fluid at a heating system heat exchanger constructed andarranged to be coupled to a heating system associated with theenclosure, moving a second heat transfer fluid through the valvearrangement, the valve arrangement constructed and arranged todistribute the second heat transfer fluid to one or more cogenerationsystem components without the first heat transfer fluid contacting thesecond heat transfer fluid, and providing space cooling to the enclosureby operation of the heat pump via the second heat transfer fluid thatabsorbs thermal energy from the enclosure at a cooling system heatexchanger constructed and arranged to be coupled to a cooling systemassociated with the enclosure.

The method may further include moving the first heat transfer fluid fromat least one of the heat engine and heat pump and through the valvearrangement in a first direction to supply thermal energy to the heatingsystem heat exchanger to provide heating to the enclosure, and movingthe first heat transfer fluid from the heating system heat exchanger andthrough the valve arrangement in a second direction opposite the firstdirection to return the first heat transfer fluid to at least one of theheat engine and the heat pump so that the first heat transfer fluidabsorbs further thermal energy from at least one of the heat engine andthe heat pump. The method may further include moving the second heattransfer fluid from the heat pump and through the valve arrangement in afirst direction to receive thermal energy from the cooling system heatexchanger to provide cooling to the enclosure, and moving the secondheat transfer fluid from the cooling system heat exchanger and throughthe valve arrangement in a second direction opposite the first directionto return the second heat transfer fluid the heat pump at which furtherthermal energy is transferred from the second heat transfer fluid to theheat pump. The method may further include moving the second heattransfer fluid from a thermal storage system heat exchanger and throughthe valve arrangement in a first direction to supply thermal energy tothe heat pump to operate the heat pump, and moving the second heattransfer fluid from the heat pump and through the valve arrangement in asecond direction opposite the first direction to return the second heattransfer fluid to the thermal storage system heat exchanger. The methodmay further include moving the second heat transfer fluid from a thermalstorage system heat exchanger and through the valve arrangement in afirst direction to supply thermal energy to heat reservoir to preventexcess ice from accumulating on the heat reservoir, and moving thesecond heat transfer fluid from the heat reservoir and through the valvearrangement in a second direction opposite the first direction to returnthe second heat transfer fluid to the thermal storage system heatexchanger.

In one other embodiment, a method of providing heating, cooling andelectricity to an enclosure using a cogeneration system may includegenerating thermal energy and electricity by operation of a heat engine,providing thermal energy by operation of a heat pump, transferringthermal energy from the heat engine and the heat pump to a first heattransfer fluid, providing at least one of space heating and waterheating to the enclosure via the first heat transfer fluid at a heatingsystem heat exchanger constructed and arranged to be coupled to aheating system associated with the enclosure, and providing thermalenergy to a thermal storage system heat exchanger via at least one ofthe first heat transfer fluid and a second heat transfer fluid, thethermal storage system heat exchanger constructed and arranged to becoupled to a thermal storage system associated with the enclosure.

The method may further include providing space cooling to the enclosurevia the second heat transfer fluid that absorbs thermal energy from theenclosure at a cooling system heat exchanger constructed and arranged tobe coupled to a cooling system associated with the enclosure. The methodmay further include supplying electricity generated by the heat engineto one or more energy suppliers. Thermal energy may be provided to thethermal storage system periodically to maintain an amount of thermalenergy stored in the thermal storage system above a threshold level.

These and additional features provided by the embodiments describedherein will be more fully understood in view of the following detaileddescription, in conjunction with the drawings.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a block diagram of a cogeneration system including a heatengine and a heat pump that provides heating, cooling, and electricityto an enclosure, in accordance with an embodiment of the presentdisclosure.

FIG. 2 is a block diagram of a cogeneration system illustrating theproduction of energy, in accordance with an embodiment of the presentdisclosure.

FIG. 3 is a schematic diagram of a cogeneration system including aBrayton-cycle heat engine and vapor compression heat pump that provideheating, cooling, and electricity to the enclosure shown in FIG. 1, inaccordance with another embodiment of the present disclosure.

FIG. 4 is a schematic diagram of a cogeneration system including aBrayton-cycle heat engine operatively coupled in series to a vaporcompression heat pump, in accordance with another embodiment of thepresent disclosure.

FIG. 5 is a schematic diagram of a cogeneration system including a vaporcompression heat pump coupled in series to a Brayton-cycle heat engineoperatively, in accordance with another embodiment of the presentdisclosure.

FIG. 6 is a schematic diagram of a cogeneration system configured tosupply space heating and electricity to the enclosure using a heatengine, in accordance with an embodiment of the present disclosure.

FIG. 7 is a schematic diagram of a cogeneration system configured tosupply water heating and electricity to the enclosure using a heatengine, in accordance with an embodiment of the present disclosure.

FIG. 8 is a schematic diagram of a cogeneration system configured tosupply space and water heating and electricity to the enclosure using aheat engine, in accordance with an embodiment of the present disclosure.

FIG. 9 is a schematic diagram of a cogeneration system configured tosupply electricity to the enclosure using a heat engine, in accordancewith an embodiment of the present disclosure.

FIG. 10 is a schematic diagram of a cogeneration system configured tosupply space heating to the enclosure using a heat pump, in accordancewith an embodiment of the present disclosure.

FIG. 11 is a schematic diagram of a cogeneration system configured tosupply water heating to the enclosure using a heat pump, in accordancewith an embodiment of the present disclosure.

FIG. 12 is a schematic diagram of a cogeneration system configured tosupply space and water heating to the enclosure using a heat pump, inaccordance with an embodiment of the present disclosure.

FIG. 13 is a schematic diagram of a cogeneration system configured tosupply space cooling to the enclosure using a heat pump, in accordancewith an embodiment of the present disclosure.

FIG. 14 is a schematic diagram of a cogeneration system configured tosupply water heating and space cooling to the enclosure using a heatpump, in accordance with an embodiment of the present disclosure.

FIG. 15 is a schematic diagram of a cogeneration system configured tode-ice the point of contact to a heat reservoir, such as an outside heatexchanger, using a heat pump, in accordance with an embodiment of thepresent disclosure.

FIG. 16 is a schematic diagram of a cogeneration system configured tosupply space heating to the enclosure using a heat pump and a thermalstorage system, in accordance with an embodiment of the presentdisclosure.

FIG. 17 is a schematic diagram of a cogeneration system configured tosupply space heating and electricity to the enclosure using a heat pump,a heat engine, and a heat reservoir, in accordance with an embodiment ofthe present disclosure.

FIG. 18 is a schematic diagram of a cogeneration system configured tosupply water heating and electricity to the enclosure using a heat pumpand a heat engine, in accordance with an embodiment of the presentdisclosure.

FIG. 19 is a schematic diagram of a cogeneration system configured tosupply space and water heating and electricity to the enclosure using aheat pump and a heat engine, in accordance with an embodiment of thepresent disclosure.

FIG. 20 is a schematic diagram of a cogeneration system configured tosupply space cooling and electricity to the enclosure using a heat pumpand a heat engine, in accordance with an embodiment of the presentdisclosure.

FIG. 21 is a schematic diagram of a cogeneration system configured tosupply water heating and space cooling and electricity to the enclosureusing a heat pump and a heat engine, in accordance with an embodiment ofthe present disclosure.

FIG. 22 is a schematic diagram of a cogeneration system configured tode-ice the point of contact to a heat reservoir and provide electricityto the enclosure using a heat pump and a heat engine, in accordance withan embodiment of the present disclosure.

FIG. 23 is a schematic diagram of a cogeneration system configured tosupply space heating and electricity to the enclosure using a heat pump,heat engine, and a thermal storage system, in accordance with anembodiment of the present disclosure.

These and other features of the present embodiments will be understoodbetter by reading the following detailed description, taken togetherwith the figures herein described. The accompanying drawings are notintended to be drawn to scale. For purposes of clarity, not everycomponent may be labeled in every drawing.

DETAILED DESCRIPTION

Systems and methods are disclosed for a cogeneration system configuredto provide heating, cooling, and/or electricity to an enclosure. Asdiscussed in more detail below, in one embodiment, the system isconfigured for use with an enclosure such as a residential, municipal,commercial, or any other type of building (e.g., a home or office). Asdiscussed below, in another embodiment, the system is configured as anauxiliary power unit (APU) and may be configured for use with anenclosure such as a vehicle (including various types of automobiles,including but not limited to long-haul trucks). In yet anotherembodiment, the system is configured as an APU and may be configured fora variety of mobile applications, including but not limited to, militarytemporary power systems, micro-grids, and boats.

As discussed in greater detail below, the system may broadly include aheat engine and a heat pump that can be operated together orindividually to supply heating, cooling, or electricity (or acombination thereof). The heat engine can provide heating or electricity(or both) to the enclosure. Thermal energy generated by the heat engine,in some examples, can also be used for process heating, for example. Thecogeneration system, in some examples, can be further configured totransfer electricity produced by the heat engine to the grid. Attachedor otherwise coupled to the heat engine is a first conduit that isfilled with a heat transfer fluid. The heat transfer fluid enablesthermal energy generated by the heat engine to be used for heating ofthe enclosure. The system further includes a heat pump that can heat orcool (or both) the enclosure. The heat pump may supply both heating andcooling to the enclosure simultaneously or one at a time. Coupled to theheat pump may be a second conduit and a third conduit that are filledwith a heat transfer fluid. The second conduit is constructed andarranged to allow thermal energy generated by the heat pump to betransferred to the enclosure for space heating and/or water heating. Thethird conduit is constructed and arranged to enable thermal energy to beabsorbed by the heat transfer fluid from the enclosure to provide spacecooling.

General Overview

Thermal power generating stations, such as those systems that include acentral power station, do not efficiently supply electricity (e.g.,generate and distribute electric power) to consumers. Many central powerstations, for example, produce electricity at an efficiency of less than50%. This poor efficiency may be caused by thermal energy losses (e.g.,rejected heat) that are inherent in the conversion of thermal energyinto electricity. The efficiency of such centralized systems may be yetfurther reduced as electricity is transmitted many miles from the sourceto the consumer. As electricity is transmitted along the network ofdistribution lines (i.e., the grid) that electrically connects theconsumer to the central power station, thermal energy losses (e.g.,heat) can occur. As a result, it is estimated that only approximately34% of the energy from the fuel processed by the central power stationmay be supplied to consumers.

Once the electricity is produced, there are also many challenges withmanaging its distribution. For instance, the distribution of electricityis typically managed using supply-side management techniques. Suchtechniques may involve generating electricity based on the needs orcircumstances of the power station rather than based on the needs orcircumstances of the consumer. For instance, a power station may produceless electricity than its rated capacity when it is more cost effectiveto do so, for example when the cost of fuel is high, or consumer demandis low. As a result, electricity is distributed based on theavailability of electricity produced by the central power station ratherthan consumer demand. Thus, there may be periods during a year, such aspeak-demand periods, in which there is not enough electricity to satisfyconsumer demands. In many such instances, users may experience a loss ofelectric power (e.g., a power blackout).

Thus, and in accordance with an embodiment of the present disclosure,systems and methods are disclosed for a cogeneration system configuredto provide heating, cooling, and/or electricity to an enclosure. Asmentioned above, the enclosure can be any type of building such as butnot limited to a stationary structure, a home, office, retail building,school, hotel and/or factory. In some other embodiments, the enclosurecan be a mobile platform, for example a camper, bus, mobile home, ortractor of a semi-trailer truck. The system includes a heat engine and aheat pump that can be operated together or individually to supplyheating, cooling, or electricity (or a combination thereof) to theenclosure. As discussed in more detail below, a heat engine, such as aclosed-loop, turbo-Brayton cycle heat engine, can provide heating orelectricity (or both) to the enclosure by processing a working fluidcontained therein to create thermal energy. In other embodiments, theheat engine can be configured differently, such as, but not limited toan Open-loop Brayton cycle (e.g., Jet Engine), an Otto-cycle gas pistonengine, a diesel engine, a steam or organic Rankine-cycle engine, fuelcell, or a Stirling engine, or a thermoelectric generator. Attached orotherwise coupled to the heat engine is a first conduit that is filledwith a heat transfer fluid, such as, but not limited to glycol or water.The heat transfer fluid, in a general sense, is a medium (e.g., a liquidor gas or other phase change material) that is capable of absorbing andtransferring thermal energy. The heat transfer fluid enables thermalenergy generated by the heat engine or the heat pump (or both) to beused for heating of the enclosure.

In one embodiment, thermal energy generated by the heat engine can alsobe stored within one or more thermal storage devices. These devicesmaintain or otherwise keep a source of thermal energy that can be usedto improve system performance. For instance, in one embodiment, thestored thermal energy can be used as a heat source by the heat pump whenthe outside temperature is low and below a level at which one couldotherwise efficiently operate the heat pump. As discussed more below, inone embodiment, the stored thermal energy can also be used for otherpurposes, such as de-icing the point of contact to a heat reservoir,such as an outside heat exchanger, or recovering of thermal energy toprevent a loss of energy to the environment and improve cogenerationsystem performance.

Furthermore, in one embodiment, the cogeneration system may beconfigured to be operated without using electricity from energysuppliers via the grid. For example, in one embodiment, the heat enginecan provide electricity to operate the heat pump. This off-the-gridoperation allows the enclosure to operate without the risk thatelectricity may not be available as so commonly occurs from thefluctuating energy requirements associated with energy suppliers. In oneembodiment, the heat engine provides electricity to operate both theheat pump and enclosure. The cogeneration system, in one embodiment, mayalso include other energy generating devices, such as, but not limitedto, solar panels, to supply electricity to operate the enclosure or theheat pump (or both). In one embodiment, the cogeneration system mayinclude one or more electrical energy storage devices, for examplebatteries or capacitors, to store energy generated by the heat engine(or other energy generation devices) for future use or as a source ofbackup electricity.

The system further includes a heat pump that is configured to heatand/or cool the enclosure (or both). In one embodiment, the heat pump isconfigured as a vapor-compression cycle heat pump, and in anotherembodiment, the heat pump may be configured as a Reverse Brayton cycle,a thermal electric, or other forms of heat pump. The heat pump cansupply both heating and cooling to the enclosure simultaneously or oneat a time by transferring thermal energy from the working fluidcontained therein to the heat transfer fluid of the system. The workingfluid generally speaking can be a gas or liquid, for example propane. Asdiscussed below, in one embodiment, coupled to the heat pump is a secondconduit and a third conduit that are each filled with a heat transferfluid. In one embodiment, the heat transfer fluid is the same fluid ineach of the first, second and third conduits of the cogeneration system.Depending on a given application, the heat transfer fluid of the secondconduit can transfer thermal energy generated by the heat pump to theenclosure for space heating and/or water heating. In addition, the heattransfer fluid of the third conduit can absorb thermal energy from theenclosure to provide space cooling, or from the surrounding environmentvia a heat reservoir to operate the heat pump. In one embodiment, theuse of the heat transfer fluid of the second and third conduits allowsfor the space cooling of some enclosed region while providing heating toanother enclosed region. Numerous cogeneration system configurationswill be apparent in light of the present disclosure.

Example Cogeneration System Application

FIG. 1 is a block diagram of a cogeneration system 10 including a heatengine 100 and a heat pump 400 that provide heating, cooling, and/orelectricity to an enclosure 500, in accordance with an embodiment of thepresent disclosure. As previously descried herein, there are manydisadvantages associated with only receiving electricity from a centralpower station. Thus, cogeneration systems of the present disclosure mayprovide a more reliable and efficient alternative to traditional centralpower electrical distribution systems. In more detail, the cogenerationsystems as described herein are configured to generate thermal andelectrical energy locally to satisfy heating, cooling, and electricitydemands of an enclosure (e.g., a home, commercial or other building, orvehicle). Thus, according to one embodiment, consumers may not need tobe dependent on a centralized power station via the grid for theirelectricity. Moreover, consumers may not need to be subject tofluctuating requirements (e.g., availability of electricity and cost)that are common with managing centralized power systems. In oneembodiment, the cogeneration systems of the present disclosure can beconnected to existing heating, cooling, and electrical distributionsystems of the enclosure. In another embodiment, the cogeneration systemmay replace existing heating and cooling systems. No matter the mannerin which it is installed, the cogeneration systems of the presentdisclosure can eliminate the necessity for separate heating and coolingsystems and backup generators. In another embodiment, the cogenerationsystem 10 can provide electricity to the grid when the cogenerationsystem 10 generates more electricity than needed by the enclosure.

In addition, the cogeneration systems as described herein may also serveas a source of electricity when there is no commercially availablesource of electricity. In one embodiment, the cogeneration system 10 canbe an auxiliary power unit for use with stationary (e.g., a home oroffice building) or mobile (e.g., a motor vehicle) platforms. In oneembodiment, the cogeneration system 10 can be configured to replaceconventional sources of backup energy, such as generators, to provideenergy during a power outage (e.g., black out). The cogeneration systemcan be configured to connect or otherwise interface with existingtemporary or auxiliary power systems of the enclosure. In otherembodiments, the cogeneration system can be configured as an auxiliarypower unit (APU) to provide energy to mobile platforms (e.g., a longhaul truck). An APU, in a general sense, can be a device that providesenergy to a motor vehicle for functions other than those that cause thevehicle to move. In some embodiments, for instance, the cogenerationsystem 10 can be used to provide heating, cooling, and/or electricity toan occupant compartment (e.g., a cab of a truck) to allow an occupant toremain comfortably in the vehicle when the primary drive engine is notoperating (e.g., not idling). Thus, heating, cooling, and/or electricitycan be provided to a compartment of the vehicle (e.g., a cab of a truckor cargo space of a trailer) without operating the primary drive engine.As a result, owners and operators of trucking lines can reduce fuelcosts, engine hours, maintenance and services costs because the primarydrive engine of the vehicle is not operating for long periods of timewhen the vehicle is not moving (e.g. overnight while the driver rests).The cogeneration system 10, in some embodiments, can provideelectricity, heating, and cooling to a long-haul truck or its trailer(or both). The cogeneration system 10, in some other embodiments, canalso provide electricity to charge one or more batteries of the vehicle.Regardless of whether commercial power is available or not, thecogeneration systems of the present disclosure provide heating, cooling,and/or electricity to the enclosure. As can be seen, broadly speaking,the cogeneration system 10 illustrated in FIG. 1 includes a heat engine100, a plurality of conduits 200, electrical cables 300, a heat pump400, and an enclosure 500. The heat engine 100 and heat pump 400, insome embodiments can be constructed and arranged as one unit or deviceheld within a common housing (as indicated by the dotted lines in FIG.1). In other embodiments, the heat engine 100 and heat pump 400 may belocated separately from one another to install or otherwise connect thecogeneration system to the enclosure 500. No matter how they areinstalled, the heat engine 100 and the heat pump 400, provide thermalenergy or electricity (or both) to the enclosure 500 via conduits 200and electrical cables 300, as described further herein.

The cogeneration system 10 includes a heat engine 100 to convert thermalenergy (e.g., heat) to work which can be used to generate electricity.The heat engine 100 processes fuel, for example wood pellets, coal, oil,propane, natural gas or other biogases, to generate thermal energy. Asthe fuel is processed or otherwise consumed, the heat engine 100produces work (e.g., mechanical work such as a rotating shaft) that canbe used to generate electricity to operate other components of thecogeneration system 10 (e.g., the heat pump 400). In one embodiment, thegenerated electricity can also be provided to a centralized powergeneration system (e.g., the grid), depending on the electricity demandsof the enclosure 500. Besides the generation of electricity, the heatengine 100 can also produce thermal energy (e.g., heat) as it processesthe fuel to generate mechanical work. This thermal energy can betransferred to one or more components of the cogeneration system 10 oran enclosure 500, as discussed further herein.

Attached to the heat engine 100 are one or more conduits 200 for thedistribution of thermal energy within the cogeneration system 10. Theconduits 200 transmit a heat transfer fluid from the heat engine 100 toone or more components of the cogeneration system 10. Heat transferfluid, in a general sense, is a medium (e.g., a liquid or gas) that iscapable of absorbing and transferring thermal energy. In one embodiment,the heat transfer fluid contains glycol. In another embodiment, the heattransfer fluid contains water. In another embodiment, the heat transferfluid is mixture of water and glycol. The conduits 200 can be filledwith a common heat transfer fluid or different conduit sections maycontain different fluids, depending on a given application. In anexample embodiment, conduits 200 may be pipes, ducts, tubing or otherplumbing systems for transporting the heat transfer fluid to the variouscomponents of the cogeneration system 10. The conduits 200 can beconstructed and arranged to create separate high-temperature and lowtemperature heat transfer fluid paths or loops. Each path can containone or more fluid pumps for moving the heat transfer fluid through theconduits 200. The heat transfer fluid may absorb thermal energy from thehigh temperature thermal energy reservoirs (e.g., heat engine 100) andtransfer it to low temperature thermal energy reservoirs (e.g., a heatexchanger). One of ordinary skill in the art will recognize that theheat transfer fluid can be moved through the cogeneration system 10using pumps, valves, diverters, or other fluid flow devices integratedwithin or otherwise connected to conduits 200. For instance, in someembodiments, the cogeneration system 10 may include a proportioningvalve to direct returning heat transfer fluid from the enclosure 500 tothe heat engine 105 and heat pump 405. As a result, the heat engine 105and heat pump 405 can operate at different outputs and thereby improvesystem efficiency. Numerous plumbing system configurations will beapparent in light of the present disclosure.

Attached to the heat engine 100 are also one or more electrical cables300 for distributing electricity generated by the heat engine 100 toother components of the cogeneration system 10. For instance, electricalcables 300 may electrically connect the heat engine 100 to heat pump 400to enable the heat pump 400 to be operated using electricity provided bythe heat engine 100. Electrical cables 300 may also connect the heatpump 400 to the enclosure 500 to provide alternate supply of electricity(e.g., the grid or storage battery) to operate the heat pump 400,depending on a given application in which the cogeneration system 10 isbeing operated.

The cogeneration system 10 includes a heat pump 400 to transfer thermalenergy (e.g., heat) from a high temperature reservoir to a lowtemperature reservoir. As one of ordinary skill in the art willappreciate, a heat pump 400 is a device that transfers thermal energyfrom a source of heat to a relatively lower temperature space or object(e.g., a thermal energy sink). In operation, the working fluid of theheat pump 400 both absorbs and transfers thermal energy. In more detail,the high-temperature working fluid of the heat pump 400 transfersthermal energy via a heat exchanger (also referred to as a condenser) toa heat transfer fluid which in turn transfers heat to enclosure 500. Inaddition, low-temperature working fluid of the heat pump 400 absorbsthermal energy from another heat transfer fluid in communication with ahigh-temperature source (e.g., are area around the enclosure 500) toenable the low-temperature working fluid to be converted to ahigh-temperature fluid, and thus provide a source of thermal energy. Toaccomplish this heat transfer process, work is put into the cogenerationsystem 10 in the form of electricity supplied to the heat pump 400.Sources of electricity for operating the heat pump 400 may include, butare not limited to, the heat engine 100, storage batteries, or the grid,depending on a given application in which the cogeneration system 10 isbeing operated.

As illustrated in FIG. 1, the cogeneration system 10 also includes anenclosure 500 that receives thermal and electrical energy from the heatengine 100 and heat pump 400. In general sense, the enclosure 500 can beany space or area, in which electricity or thermal energy (or both) isused to, for example, operate electrical appliances. In an exampleembodiment, the enclosure 500 is a residence, such as a single familyhome. In other embodiments, the enclosure 500 can be any type ofbuilding or structure, such as, but not limited to, a church, a schoolor other government building, a multiple-family structure (e.g., anapartment or condominium building), retail (e.g., a department store orrestaurant), or commercial structure (e.g., an office building orfactory). The enclosure 500, in yet other embodiments, can be a mobileplatform, such as a motor vehicle, a camper, bus, mobile home, or along-haul truck (e.g., a semi-trailer truck). The thermal energygenerated by the heat engine 100 or heat pump 400 (or both) istransferred to the enclosure components via the heat transfer fluidcarried by a number of conduits 200 and other plumbing systemcomponents. Similarly, electrical energy provided by the heat engine 100is transferred to one or more components of the enclosure 500 viaelectrical cables 300. Some of the conduits 200 function as supply andreturn lines to move heat transfer fluid between the enclosure 500 andthe heat engine 100 or heat pump 400 (or both). The conduits 200 andelectrical cables 300 have been previously described herein. Numerousother enclosure configurations will be apparent in light of the presentdisclosure.

FIG. 2 is a block diagram of a cogeneration system 10 illustrating theproduction of energy, in accordance with an embodiment of the presentdisclosure. In general, the cogeneration system 10 of the presentdisclosure can supply energy to satisfy heating, cooling, andelectricity demands for an enclosure (e.g., a home or office building)while using significantly less energy as compared to present systems (orcombination of systems) currently available in the marketplace. Forinstance, as described herein, in one particular embodiment, thecogeneration system 10 can operate using between 20 to 50 percent lessenergy than present systems. In an example embodiment, the heat engine100 can generate up to 5 kilo-watt (kW) of electricity usingapproximately 13.9 kW of fuel (e.g., oil, natural gas, or propane). Ascan be seen, the fuel consumed by the heat engine 100 is converted toboth thermal (e.g., 8.9 kW) and electrical (e.g., 5.0 Kw) energy. Someof the thermal energy (e.g., 1.4 kW) is waste or unused heat that istransferred to an area outside the enclosure 500 (e.g., the surroundingenvironment) during heat engine operation. The remainder of the thermalenergy (e.g., 7.5 kW) can be transferred to the enclosure for purposesof space heating or water heating (or both). Besides thermal energy, theheat engine 100 may also produce electrical energy in the form ofelectricity. As can be seen, the heat engine 100 can generateelectricity (e.g., 5 kW) that can be used to supply electricity to theheat pump 400 or enclosure 500. Once received, the heat pump 400 usesthe electricity from the heat engine 100 to generate thermal energy. Inoperation, the heat pump 400 absorbs thermal energy (e.g., 6.8 kw) fromthe surrounding environment to produce thermal energy (e.g., 10.8 kW)that can be used to supply space heating or water heating (or both) tothe enclosure 500. In one example, the cogeneration system may receivethermal energy directly from environment (e.g., thermal energy storedwithin a heat reservoir such as a body of water or in the ground). Insuch instances, conduits of the cogeneration system may be in contactwith a heat reservoir, such as a lake or stream within the environmentor a portion of the ground beneath the environment, to receive thermalenergy therefrom. In other examples, the cogeneration system mayindirectly receive thermal energy from the environment by using, forexample, a heat exchanger, as will be described further herein. Thecogeneration system 10 can produce approximately 18.3 kW of thermalenergy (at a temperature of the environment of −10° C.) and 1 kW ofelectricity for use by the enclosure 500. As can be seen, thecogeneration system 10 may be configured to provide enough energy(thermal and electrical energy) to the enclosure 500 without usingelectricity from an energy supplier via the grid. Thus, the cogenerationsystem 10 may be used for off-grid operation. In one embodiment,however, the cogeneration system 10 can also serve as an energy sink(e.g., an energy consumer) or energy source (e.g., an energy provider)for the grid in response to fluctuating requirements of availableenergy, as will be described further herein.

Example Heat Engine and Heat Pump Cogeneration Systems

FIG. 3 is a schematic diagram of a cogeneration system 15 including aclosed-loop Brayton cycle heat engine 105 (hereinafter referred to asheat engine 105) and vapor compression heat pump 405 (hereinafterreferred to as heat pump 405) to provide heating, cooling, andelectricity to the enclosure 500 shown in FIG. 1, in accordance withanother embodiment of the present disclosure. Attached or otherwisecoupled to the heat engine 105 is a first conduit 200A that is filledwith a heat transfer fluid to enable thermal energy generated by theheat engine to be used for heating of the enclosure. The heat transferfluid may be a first heat transfer fluid. Coupled to the heat pump 405is a second conduit 200E and a third conduit 200F that are also filledwith a heat transfer fluid. The second conduit 200E is constructed andarranged to allow thermal energy generated by the heat pump 405 to betransferred to the enclosure for space heating and/or water heating. Thethird conduit 200F is constructed and arranged to enable thermal energyto be absorbed by the heat transfer fluid from the enclosure to providespace cooling. The heat transfer fluid associated with the secondconduit 200E may be the first heat transfer fluid associated with thefirst conduit 200A, and the heat transfer fluid associated with thethird conduit 200F may be a second heat transfer fluid. The firstconduit 200A and the second conduit 200E may be fluidly coupled andconfigured to at least one of proportion and thermally isolate the firstheat transfer fluid between the first conduit 200A and the secondconduit 200E. The first heat transfer fluid may be proportioned betweenthe first conduit 200A and the second conduit 200E through a valvearrangement 510, as described in greater detail further below.

As can be seen, the heat engine 105 and heat pump 405 are connected inparallel with one another via conduits 200A and 200E so that the heattransfer fluid can flow in separate paths to each component. This typeof configuration allows the cogeneration system 15 to move the heattransfer fluid without experiencing thermal energy losses caused bymoving the heat transfer fluid through the heat engine 105 or heat pump405 when they are not operating. In an example embodiment, thecogeneration system 15 can include a heat engine 105, heat pump 405 andan enclosure 500.

Heat Engine

The cogeneration system 15 includes a heat engine 105 to generate heatand electricity to operate one or more other components of the system 15(e.g., the heat pump 405). In some embodiments, a closed-loopBrayton-cycle heat engine, such as heat engine 105, provides severaladvantages over other types of heat engines. These advantages caninclude, for instance, higher efficiency, smaller mass and size, longerintervals between engine maintenance, undetectable vibration, andflexible packaging. The heat engine 105, in an example embodiment, is aturbo machine and capable of generating up to 5 Kilowatts (kW). In otherembodiments, the heat engine 100 can be an Open-loop Brayton cycle(e.g., Jet Engine), an Otto-cycle gas piston engine, a diesel engine, asteam or organic Rankine-cycle engine, fuel cell, or a Stirling engine,or a thermoelectric generator. The type of heat engine implemented inthe cogeneration system 15 can be selected based on a number of factorsincluding electric efficiency, emissions, fuel flexibility, andturn-down ratio, depending on a given application. As can be seen, theheat engine 105 includes a thermal source 110, an expander 120, heatengine recuperator 130, heat exchanger 140, compressor 150, thermalsource recuperator 160, and generator 170.

The heat engine 105 includes a thermal source 110 to transfer thermalenergy to a working fluid of the heat engine 105. The thermal source 110operates as a thermal reservoir to raise the temperature of the workingfluid as it contacts the thermal source 110. A working fluid can be agas or liquid that actuates or otherwise operates a machine. In anexample embodiment, the thermal source 110 is a combustor that includes,for example a burner and a combustion chamber. The thermal source 110can generate thermal energy through combustion of fuel (e.g., fossil orrenewable fuels). Attached to the thermal source 110 are fuel tube 113,air intake tube 116, and exhaust tube 119 to promote the combustion offuel by the burner within the combustion chamber of the thermal source110. The fuel tube 113 is adapted to supply fuel, such as such as oil,propane, or natural gas to the combustion chamber of the thermal source110. In some other embodiments, the fuel tube is configured to supplyrenewable fuels, such as biofuels including for example wood pellets andBioMass or BioFuels (bio gas, bio oil), renewable fuels. As can be seen,an air intake tube 116 is also attached to the thermal source 110. Theair intake tube 116 is adapted or otherwise configured to supply air tothe thermal source 110 to enable combustion of the fuel therein. Oncethe fuel has been consumed, the exhaust gases can leave the thermalsource via an exhaust tube 119 attached thereto. The exhaust tube 119 isconfigured to carry the exhaust gases from the thermal source 110 to thesurrounding environment. Numerous other thermal source configurationswill be apparent in light of the present disclosure.

The heat engine 105 includes an expander 120 for changing the pressureof the working fluid from a high pressure to a low pressure. In anexample embodiment, the expander 120 is a turbo expander, such as aradial flow turbine, in which high pressure gas is expanded to producework, such as mechanical movement of a shaft. The output work of theexpander 120 can be used to operate the compressor 150 to compress theworking fluid at another point during the operating cycle of the heatengine 105. In addition, the work generated by the expander 120 can beused to operate the generator 170 to produce electricity, as will bedescribed further herein. The expander 120, in some other embodiments,can be an axial flow turbine or positive displacement mechanism. As itproduces work via the expander 120, the pressure of the working fluid isreduced to a lower pressure, but maintains a relatively high temperatureas compared to the surrounding environment. The efficiency of the heatengine 105 can thus be improved by transferring some of this thermalenergy from the low-pressure working fluid to the high-pressure workingfluid presently further along in the closed cycle of engine 105.

The heat engine 105 includes a heat engine recuperator 130 (hereinafterreferred to as recuperator 130) to transfer thermal energy from the hightemperature working fluid that exits the expander 120 to other lowtemperature working fluid. In a general sense, the recuperator 130 is adevice for recovery of waste thermal energy (e.g., heat). In an exampleembodiment, the recuperator 130 recovers or otherwise absorbs thermalenergy from the high-temperature working fluid that exits the expander120 and transfers it to other low-temperature working fluid prior toentering the thermal source 110. As a result, the overall efficiency forthe heat engine 105 is improved because less fuel is consumed by thethermal source 110 because the working fluid entering the source 110 isat a higher temperature. In an example embodiment, the recuperator 130is a vertical flat panel counter-flow heat exchanger that physicallyseparates the high-temperature working fluid from the low-temperatureworking fluid. In operation, the high-temperature working fluid flowsthrough the recuperator 130 and contacts one surface, such as a wall orpanel. As a result of this contact, the panel absorbs thermal energyfrom the high-temperature working fluid by way of convection. Thisthermal energy is transferred through the wall via conduction, and isabsorbed by the low temperature working fluid in contact with anopposing surface of the panel. In another embodiment, the recuperator130 can be a counter-flow heat exchanger, such as a horizontal flatpanel or cellular type heat exchanger. Although thermal energy has beenabsorbed from the high-temperature working fluid, there can still beadditional thermal energy that can be recovered therefrom. Thus,efficiency of the heat engine 105 can yet further be improved uponrecovery of this additional thermal energy.

The heat engine 105 further includes a heat exchanger 140 fortransferring thermal energy (e.g., heat) from the working fluid of theheat engine 105 to the heat transfer fluid of the cogeneration system15. As described above, the working fluid exiting the heat enginerecuperator 130 contains thermal energy that is removed from the workingfluid (and heat engine) which can be used elsewhere within thecogeneration system 15 (e.g., to heat the enclosure 500) or rejected toa heat reservoir. In a general sense, heat exchanger 140 can be a devicefor transferring thermal energy between a solid object and a fluid orbetween two or more fluids. In some applications, the two or more fluidscan be separated by a barrier (e.g., a wall, piping or a panel) toprevent mixing of the fluids. In other applications, the fluids can bein direct contact with each other (e.g., mixed together). In an exampleembodiment, heat exchanger 140 is a shell and tube heat exchanger. Insuch an embodiment, the heat exchanger 140 enables thermal energy to beabsorbed from the working fluid of the heat engine 105 and transferredto the heat transfer fluid of the cogeneration system 15 to providethermal energy (e.g., heat) to the enclosure 500, as will be describedin more detail herein. In other embodiments, the heat exchanger 140 canbe a plate, or a plate and shell heat exchanger. No matter itsparticular configuration, the heat exchanger 140 reduces the amount ofunrecovered thermal energy (e.g., waste heat) produced by the engine105, and thus improves the overall efficiency of the heat engine 105.

The heat engine 105 further includes a compressor 150 for moving theworking fluid from a low pressure to a high pressure. In a generalsense, the compressor 150 can be a mechanical device that increases thepressure of a gas by reducing a volume in which the gas is contained. Asdescribed above, the working fluid entering the compressor 150 is at alow pressure (e.g., atmospheric pressure) upon flowing through theexpander 120. To compress the working fluid, work is inputted into thecogeneration system 15. In an example embodiment, the compressor 150receives an input (e.g., mechanical work in the form of rotating shaft)from the expander 120. As a result of moving the working fluid throughthe compressor 150, the pressure of the working fluid is significantlyincreased, but the temperature of the working fluid has only slightlyincreased. Thus, the working fluid can move to the thermal source 110 atwhich its temperature is increased, and thereby readying the fluid forthe next heat engine operating cycle.

The heat engine 105, in some embodiments, can include a thermal sourcerecuperator 160, to transfer thermal energy from the exhaust gaseswithin the exhaust tube 119 to low temperature air flowing through theair intake tube 116. In a general sense, the thermal source recuperator160 is a device for recovery of waste thermal energy (e.g., heat), suchas a heat exchanger. In more detail, the thermal source recuperator 160recovers or otherwise absorbs thermal energy from exhaust gases flowingthrough the exhaust tube 119 and transfers it to the low-temperature airflowing through the air intake tube 116, and subsequently entering thethermal source 110. As a result, the overall efficiency for the heatengine 105 is improved, because less fuel is used to raise thetemperature of the working fluid since the air entering the thermalsource 110 is at a higher temperature than the ambient air temperatureof the surrounding environment.

The heat engine 105 also includes a generator 170 for producingelectricity using the output of work provided by the expander 120. In ageneral sense the generator 170 is a device that converts mechanicalenergy (e.g., a rotating shaft) into electrical energy for use. In anexample embodiment, the generator 170 may be a variable speed generatorhaving an operating range of 50,000 to 80,000 revolutions per minute(RPM) and capable of producing up to 5 kW of electric power. Thegenerator 170, in some other embodiments, can be a dynamo type generatorthat produces direct current using a permanent magnet field and acommutator. In other embodiments, the generator 170 can be a directcurrent or an alternating current generator having a coil of wirerotating in a magnetic field to produce electricity. Numerous othergenerator configurations will be apparent in light of the presentdisclosure.

Heat Pump

The cogeneration system 15 also includes a heat pump 405 to supply orremove thermal energy (e.g., heat) to or from the enclosure 500. Aspreviously discussed, the heat pump 405 is configured to provide thermalenergy (e.g., heat) to the enclosure 500. In an example embodiment, theheat pump 405 is an advanced vapor-compression cycle heat pump. In somesuch embodiments, the heat pump 405 is a two-stage compression cycleheat pump. The heat pump 405, in yet other embodiments, can be a solidstate or other chemical reactive process for absorption or adsorption ofthermal energy. Regardless of its configuration, the heat pump 405 mayoperate in a temperature range of between −10° Celsius (C) and 15° C. Insome applications, note that the heat pump 405 can provide thermalenergy to the enclosure 500 despite ambient outside temperatures beingas low as −30° C. As a result, the cogeneration system 15 can beinstalled and operated in the vast majority of the country in whichheating systems are operated.

The heat pump 405 contains a working fluid that absorbs thermal energyfrom one thermal energy reservoir and transfers it to another. A workingfluid generally speaking can be a gas or liquid that is actuated by amachine. In an example embodiment, the working fluid of the heat pump405 is propane. Propane offers several advantages over syntheticmaterials including lower cost, less toxicity, and reduced environmentalimpact. In some other embodiments, the working fluid can be arefrigerant. No matter its working fluid, the heat pump 405 can beconfigured, such as with hermetically seal packaging, to prevent theworking fluid from contaminating or otherwise contacting the surroundingenvironment. Such packaging allows the heat pump 405 to be safelyoperated with a number of different working fluids and outside theenclosure 500. In contrast, traditional heat pump systems move workingfluid through the enclosure. As result, traditional heat pumps have alimited number of working fluids that can be safely used within theenclosure. The heat pump 405 of the present disclosure is not solimited. In more detail, the heat pump 405 can use a number of differenttypes of working fluids because it may be sealed and packaged to preventloss of fluid to the surrounding environment. In addition, the workingfluid of the heat pump 405 can remain outside the enclosure 500 where itcan be safely used and contained such that it does not pose a danger tooccupants within the enclosure 500. As a result, less working fluid isused by heat pump 405, because the working fluid remains in the pump 405rather than being moved to transfer thermal energy to the enclosure 500.

The heat pump 405 may include an electric motor 410, a compressor 420, acondenser 430, a reducing valve 440, and an evaporator 450. In a generalsense, electric motor 410 converts electricity (e.g., electricity fromthe generator 170) into mechanical work (e.g., a rotating shaft). Theoutputted work from the electric motor 410 can be used to operate thecompressor 420, as will be described further herein. In an exampleembodiment, the electric motor 410 is alternating current (AC) electricmotor. Electric motor 410, in some embodiments, is a direct current (DC)electric motor. No matter its configuration, the electric motor 410 isto provide work to operate the heat pump 405.

As can be seen, the heat pump 405 is coupled to or otherwise connectedto the heat engine 105 to receive electricity via the generator 170 andelectrical cables 300. In one embodiment, when operating, the heatengine 105 can supply electricity to power the heat pump 405, and thusavoid using electricity from a supplier (e.g., the grid), which can beexpensive, or not always available. The cogeneration system 15 can alsobe alternatively configured to electrically connect the heat pump 405 tothe grid and/or one more electrical storage systems via electricalcables 300 to receive electricity from a source other than the heatengine 105 when operating the heat engine 105 may not be desirable orpracticable.

The heat pump 405 further includes a compressor 420 to increase thepressure and temperature of the working fluid of the heat pump 405. In ageneral sense, note that the compressor 420 can be a mechanical devicethat increases the pressure of a gas by reducing a volume in which thegas is contained. The compressor 420, in other words, can be a devicethat moves the working fluid from a low pressure to a high pressure. Inoperation, the compressor 420 receives an input from the electric motor410, such as work. It is this work that can be used to operate thecompressor 420 in which to compress the working fluid. In an exampleembodiment, the compressor 420 can be a scroll compressor. Thecompressor 420, in some other embodiments, can be a rotary piston orreciprocating piston compressor. In operation, the working fluid entersthe compressor 420 with a relatively low pressure and temperature. Oncecompressed, the working fluid (e.g., a propane gas) experiences anincrease in temperature and pressure.

In one embodiment with a vapor compression-type heat pump, the heat pump405 may further includes a condenser 430 to transfer thermal energy fromthe working fluid of the heat pump 405 to a heat transfer fluid of thecogeneration system 15. Generally speaking, the condenser 430 can be adevice, for example a heat exchanger, which is configured to transfer ofthermal energy from one fluid or solid to another. As described above,the working fluid exits the compressor 420 and contains an amountthermal energy. This thermal energy can be used elsewhere within thecogeneration system 15, such as to heat the enclosure 500. In moredetail, the condenser 430 absorbs thermal energy from the working fluidand transfers it to the heat transfer fluid. As a result, thetemperature of the heat transfer fluid increases so that it can be usedto provide heat (e.g., space or water heating) to the enclosure 500. Onthe other hand, the temperature and pressure of the working fluiddecreases as a result of the transfers of thermal energy to the heattransfer fluid. In an example embodiment, the condenser 430 is a shelland tube heat exchanger. The working fluid and heat transfer fluid, insuch embodiments, can be separated by a barrier (e.g., a wall, piping ora panel) to prevent mixing of the fluids. In other embodiments, thecondenser 430 can be a plate or a plate and shell heat exchanger.Numerous other condenser configurations will be apparent in light of thepresent disclosure.

In one embodiment, the heat pump 405 may also include a pressurereducing valve 440 (also known as an expansion valve) to decrease orotherwise lower the pressure of the working fluid. The pressure reducingvalue 440, in a general sense, can be a device that reduces the inputpressure of a fluid to a particular value at its output, therebyregulating the flow of the fluid. As described above, the working fluidexits the condenser 430 at a pressure greater than atmospheric. To readythe working fluid for the next operating cycle, the pressure of theworking fluid within the heat pump 405 is to be reduced. The workingfluid can flow or otherwise pass through the pressure reducing valve 440to reduce its pressure. In addition, the temperature of the workingfluid also decreases as the working fluid expands while moving throughthe reducing valve 440.

In one embodiment with a vapor compression-type heat pump, the heat pump405 may further include an evaporator 450 that enables the working fluidto absorb thermal energy from another thermal energy source orreservoir. Broadly speaking, the evaporator 450 can be a device, forexample a heat exchanger, which is configured to transfer thermal energyfrom one fluid to another. In an example embodiment, the evaporator 450is a shell and tube heat exchanger configured to transfer thermal energyfrom the heat transfer fluid of the cogeneration system 15 to theworking fluid of the heat pump 405. In such embodiments, the workingfluid and heat transfer fluid can be separated by a barrier (e.g., awall, piping or a panel) to prevent mixing of the fluids. In otherembodiments, the evaporator 450 can be a plate or a plate and shell heatexchanger. As described above, upon exiting the reducing valve 440 thetemperature of the working fluid has been reduced. To raise itstemperature, the working fluid can flow or otherwise move through theevaporator 450. In more detail, the evaporator 450 absorbs thermalenergy from the heat transfer fluid and transfers it to the workingfluid. As a result, the temperature and pressure of the working fluidincreases.

The heat pump 405 also includes a heat reservoir, such as an outsideheat exchanger 460 to transfer thermal energy from the surroundingenvironment to the heat transfer fluid. As previously described, theheat exchanger can be a device configured to transfer thermal energyfrom one fluid or gas to another. In an example embodiment, thecogenerations system 15 includes an outside heat exchanger 460, such asshell and tube heat exchanger, configured to function as a heat sourceor heat sink, depending on a given application. A heat source is amedium or device that transfers thermal energy to another, while a heatsink absorbs thermal energy from another medium or device. In moredetail, the heat reservoir can transfer thermal energy from ambient airto the heat transfer fluid, and thereby function as a heat source thatincreases the temperature of the heat transfer fluid. In otherembodiments, the thermal energy can be transferred from the heattransfer fluid to the ambient air via the outside heat exchanger 460. Insuch embodiments, the heat exchanger 460 can function as a heat sinkthat absorbs thermal energy from the heat transfer fluid to transfer andrelease to the ambient air. As a result of the heat sink, thetemperature of the heat transfer fluid decreases. In addition, note thatsingle or common heat exchanger configurations reduce bothmanufacturing/installation costs and complexity of the system ascompared to systems having multiple outdoor heat exchangers. In otherembodiments, the heat exchanger 460 can be a plate or a plate and shellheat exchanger. In such an embodiment, the outside heat exchanger 460can operate using low pressure heat transfer fluid. In yet otherembodiments, the cogeneration system 15 can include more than one heatreservoir, depending on the giver application. The heat reservoir, insome other embodiments, can be or otherwise integrated with a geothermalsystem to transfer thermal energy to and from the ground. In operation,the heat transfer fluid exits the evaporator 450 at temperature lowerthan the ambient air temperature of the surrounding environment. Theheat transfer fluid can then flow through the heat exchanger 460, inwhich it absorbs thermal energy from the ambient air. As a result, thetemperature of the heat transfer fluid increases, thereby allowing it tosupply thermal energy to the working fluid of the heat pump 405 at theevaporator 450 for the next cycle, as previously described herein.

In some embodiments, the heat pump 405 can be configured to receivethermal energy from a surrounding environment without an outdoor heatexchanger. In such an instance, one or more conduits in fluidcommunication with the heat pump 405 can be installed in the environmentso that the conduits are in contact with a heat reservoir (e.g., buriedunderground or in a body of water) present in the environment. Thermalenergy (e.g. geothermal energy) from the heat reservoir is transferredto the conduit and low-temperature heat transfer fluid moving therein toincrease the temperature of the fluid. The higher-temperature heattransfer fluid can flow back via one or more conduits to operate theheat pump 405. Numerous other ways of transferring thermal energy toheat transfer fluid for operating the heat pump will be apparent inlight of the present disclosure.

Enclosure

As mentioned above, in one embodiment, the cogeneration system 15further includes an enclosure 500, in which thermal energy andelectricity generated by the heat engine 105 and heat pump 405 can besupplied thereto for purposes of supplying heating, cooling, and/orelectricity. As can be seen in FIG. 3, the enclosure 500 may include avalve arrangement 510 (including but not limited to a manifold), aninside heat exchanger 520, a thermal storage system 530, a power panel540, an electric grid meter 550, an electric grid isolation switch 560,an control panel 570, an electrical energy storage system 580, and/orsolar energy panels 590. The valve arrangement 510 can be configured toselectively couple to one or more conduits 200 to receive the heattransfer fluid flowing from the heat engine 105 or heat pump 405 (orboth). In general, the valve arrangement 510 can be one device, such asa valve block, or a group of devices, such as a group of individualvalves, that guide or otherwise direct the flow of the heat transferfluid throughout the cogeneration system 15. As illustrated in FIG. 3,the valve arrangement 510 is connected to one or more conduits 200 thatform a plumbing system for moving the heat transfer fluid throughout thecogeneration system 15. In more detail, upon receiving the heat transferfluid, the valve arrangement 510 can be configured to selectivelytransfer heat transfer fluid (e.g., by diverting or otherwise directingthe flow of fluid) to one or more components of the cogeneration system,as will be described further herein. In one embodiment, the valvearrangement 510 creates a separate piping system that separates the heattransfer fluid from the heat engine 105 and heat pump 405 from othersystem conduits. The heat transfer fluid received from the heat engine105 or heat pump 405 (or both) may exit the valve arrangement 510 in atleast one direction (e.g., in a supply direction) to other cogenerationsystem components. Similarly, heat transfer fluid from othercogeneration system components may exit the valve arrangement 510 in atleast one other direction (e.g., in a return direction) to the heatengine 105 or heat pump 405 (or both) to repeat the heating or coolingcycle, depending on a given application. Regardless of itsconfiguration, the valve arrangement 510 directs heat transfer fluidmovement between the various components of the cogeneration system 15.

The enclosure 500 may include one or more inside heat exchangers tosupply heating or cooling to the enclosure. In one illustrativeembodiment, the enclosure includes inside heat exchangers 520A and 520B(collectively 520) located within or adjacent to, the enclosure 500 tosupply heating or cooling thereto. As previously described herein, aheat exchanger, in general, can be a device that transfers thermalenergy, for example, from one fluid to another. As can be seen, the heatexchangers 520 are connected to one or more conduits 200 to receive andtransfer heat transfer fluid between the heat exchangers 520 and theheat engine 105 or heat pump 405 (or both) via the valve arrangement510. Depending on a given application, the heat exchanger 520A (e.g., aheating system heat exchanger) may enable the thermal energy to beabsorbed from the heat transfer fluid and transferred to the surroundingenvironment within the enclosure 500 to heat the enclosure. In such aninstance, the heat transfer fluid can have a higher temperature than theambient air temperature of the enclosure 500, because the heat transferfluid has received thermal energy from the heat engine 105 or heat pump405 (or both). Thus, the cogeneration system 15 is operating to heat theenclosure 500. In other applications, the heat transfer fluid can absorbthermal energy from ambient air within the enclosure 500. In such anapplication, the heat transfer fluid can have a lower temperature thanthe ambient air temperature of the enclosure 500, because the heattransfer fluid moving through the heat exchanger 520B (e.g., a coolingsystem heat exchanger) has transferred some of its thermal energy to theworking fluid of the heat pump 405, as previously described furtherherein. The cogeneration system 15, for such applications, is operatingto cool the enclosure 500. In one embodiment, the heat exchanger 520Amay be part of an existing heating system for the enclosure 500 and thecogeneration system may be retrofitted to the existing heating system.Likewise, in one embodiment, the heat exchanger 520B may be part of anexisting cooling system for the enclosure and the cogeneration systemmay be retrofitted to the existing cooling system. In anotherembodiment, one or both of the heat exchangers 520A, 520B may be acomponent of the cogeneration system, and the cogeneration system mayfurther include a heating system and/or a cooling system for theenclosure.

In an embodiment, the valve arrangement 510 is configured to switchbetween operating modes to heat or cool at least a portion of theenclosure 500 while simultaneously effective opposite operating modes tocool or heat another portion or component of the enclosure 500 oranother component of the cogeneration system. As a non-limitingembodiment, the cogeneration system may heat the enclosure 500 whilesimultaneously cooling a pool within the enclosure 500, or vice versa.As another non-limiting example, such as on a cold day, a firstoperating mode of the valve arrangement 510 may direct the cogenerationsystem to heat the enclosure 500 through the heat exchanger 520A,configured to enable thermal energy to be absorbed from a first heattransfer fluid of the first conduit 200A and/or second conduit 200E andtransferred to the enclosure 500 to heat the enclosure 500. The firstoperating mode of the valve arrangement 510 may simultaneously directthe cogeneration system to use a heat reservoir such as the outside heatexchanger 460 as a heat source, such that thermal energy from the secondheat transfer fluid of the third conduit 200F that has a temperaturebelow ambient air absorbs thermal energy from the outside heat exchanger460 to increase the temperature of the second heat transfer fluid. Thevalve arrangement 510 may switch between the first operating mode and asecond operating mode, opposite the first operating mode. By way ofexample, and not as a limitation, such as on a hot day, the secondoperating mode of the valve arrangement 510 may direct the cogenerationsystem to cool the enclosure 500 through the heat exchanger 520B,configured to enable thermal energy to be absorbed from the enclosure500 and transferred to the second heat transfer fluid of the thirdconduit 200F to cool the enclosure 500. The second operating mode of thevalve arrangement 510 may simultaneously direct the cogeneration systemto use the outside heat exchanger 460 as a heat sink, and the first heattransfer fluid that has a temperature above ambient air may be absorbedby the outside heat exchanger 460 to decrease the temperature of thefirst heat transfer fluid.

The enclosure 500 further includes a thermal storage system 530 locatedwithin or adjacent to the enclosure 500. In a general sense, in oneembodiment, the thermal storage system 530 is a device (or combinationof devices) in which thermal energy is stored and made available for useat a later time. As can be seen, the thermal storage device 530 may beconnected to a plurality of conduits 200 to move heat transfer fluid toand from the device 530 to other components of the cogeneration system15. Depending on a given application, the thermal storage system 530 canhouse or otherwise contain low or high temperature heat transfer fluidfor purposes of supplying cooling or heating to the enclosure, as willbe described further herein. Thus, the thermal storage system 530 canfunction as a heat source or a heat sink, as will be described furtherdetail herein. As set forth above, a heat source is a medium or devicethat transfers thermal energy to another. A heat sink, on the otherhand, absorbs thermal energy from another medium or device. In oneexample embodiment, the thermal storage system 530 is a fluid storagetank (e.g., hot water storage tank) that includes a heat exchanger(e.g., a thermal storage system heat exchanger) disposed therein. As theheat transfer fluid passes through the heat exchanger, either thermalenergy is transferred to the fluid within the tank to heat the fluid(e.g., to heat water) or thermal energy is absorbed from the fluidwithin the tank to heat the heat transfer fluid, depending on the givenapplication. As a result, the fluid in the storage tank is either heatedor cooled by the flow of the heat transfer fluid through the heatexchanger. In other embodiments, the thermal storage system 530 can bephase change materials. Numerous other thermal storage systemconfigurations will be apparent in light of the present disclosure. Thethermal storage system 530 may include one or more heat exchangers. As anon-limiting first embodiment, the thermal storage system 530 mayinclude a storage heat exchanger configured to store a heated or cooledmedium for the thermal storage system 530. As a non-limiting secondembodiment, the thermal storage system 530 may include a domestic watersupply heat exchanger configured to heat or cool domestic water, such asfor a shower in the enclosure 500. As a non-limiting third embodiment,the thermal storage system 530 may include two heat exchangers, onebeing a storage heat exchanger and the other being a domestic watersupply heat exchanger.

The enclosure 500 also includes an electrical panel 540, electrical gridmeter 550, and an electrical grid isolation device 560. As previouslydescribed herein, the enclosure 500 may receive electricity from anelectrical power supplier via a network of transmission and distributionlines, otherwise known as the electric grid, to satisfy its electricitydemands. In a general sense, enclosures 500, such as homes or officebuildings, can include an electric grid meter 550 to transferelectricity from the grid to an electrical panel 540 of the enclosure500. The electrical panel 540 is configured to distribute theelectricity received to various locations throughout the enclosure 500to operate electrical appliances therein. In some embodiments, however,the cogeneration system 15 can be configured to supply electricity tothe enclosure 500 rather than using electricity received from the grid.In such instances, the enclosure 500 can be disconnected or otherwiseisolated from the grid to avoid transmitting electricity to the grid andthereby causing damage thereto. Thus, to avoid causing damage to thegrid, the enclosure 500 can also include an electrical grid isolationdevice 560. The electrical grid isolation device 560, in general, can bea device that breaks or otherwise disrupts an electrical connectionbetween the power panel 540 and electrical meter 550. Furthermore, theelectrical grid isolation device can also be used to electricallyisolate the enclosure from the electric grid when the grid is notoperating properly. In an example embodiment, the electrical gridisolation device 560 can be a switch that can be physically operated toelectrically isolate the enclosure 500 from the grid. In otherembodiments, the electrical grid isolation device can be an electricaldisconnect or electronic switching mechanism.

In one embodiment, the enclosure 500 may also include a control panel570 for operating cogeneration system components to manage the transferof electricity and thermal energy to satisfy demands of the enclosure500. In an example embodiment, the control panel 570 can be acombination of hardware, software, or firmware that is used to operatethe cogeneration system 15 and monitor its performance. As illustratedin FIG. 3, the control panel 570 is connected to one or more electricalcables 300 to operatively couple the panel 570 to components of thecogeneration system 15. In more detail, the control panel 570 cangenerate and transmit electrical signals to control or otherwise operatesystem components, for example, heat engine 105 or heat pump 405. Thecontrol panel 570 may include a transceiver (e.g., a router or cellularcommunication device) for receiving or transmitting information via awired or wireless network (e.g., a local area network or the internet).For instance, in one embodiment, the control panel 570 may receiveelectricity prices from electrical energy suppliers in real time, and inturn determine how to operate the cogeneration system 15 to mosteffectively and efficiently satisfy the electrical demands of theenclosure 500. In addition, the control panel may also include agraphical user interface to allow it to be configured or otherwiseaccessed during installation or operation of the system. Numerous othercontrol panel configurations will be apparent in light of the presentdisclosure.

As illustrated in FIG. 3, in one embodiment, the enclosure 500 mayfurther include an electrical energy storage system 580. Broadlyspeaking, the electrical energy storage system 580 is a device (orcombination of devices) in which electricity is stored or otherwisemaintained and made available for future use, such as in off-grid use tostart the cogeneration system and/or to meet demand fluctuations toallow heat engine to run at relatively constant output. As can be seen,the cogeneration system 15 may include one or more electrical energystorage systems 580 that are electrically connected to other devices ofthe system 15 via electrical cables 300. In operation, the cogenerationsystem 15 can be configured to transfer electricity, for example fromthe generator 170 or solar energy panels 590, to the electrical energystorage system 580 in which electricity can be stored to provide abackup source of electricity. Then, depending on a particularapplication, electricity can be transferred from the electrical energystorage system 580 to one or more cogeneration system components, forinstance electric motor 410 to operate the heat pump 405 or supplyelectricity to the power panel 540. Electricity from the electricalenergy storage system 580 may be used in a number of instancesincluding, for example, when electricity is not available from the grid(e.g., a power outage) or when the cost of electricity supplied by thegrid is high (e.g., during peak demand periods).

As shown in the embodiment illustrated in FIG. 3, the enclosure 500 mayalso include one or more solar energy panels 590 that provide a source arenewable electrical energy. In a general sense, note that solar panelsare devices configured to absorb or otherwise receive energy (e.g.,radiation in the form of light rays) from an external source of energy(e.g., the sun) and transfer that energy into heat or electricity. Ascan be seen, solar energy panels 590 can be connected to one or moreother cogeneration system components, for example, to electrical energystorage systems 580 via electrical cables 300. The solar energy panels,in some other embodiments, can also interface with one or more conduits200 to transfer thermal energy to heat transfer fluid flowingtherethrough. In an example embodiment, the solar energy panels arephotovoltaic modules that include photovoltaic solar cells.

FIG. 4 is a schematic diagram of a cogeneration system 15 including aclosed-loop Brayton cycle heat engine 105 operatively coupled viaconduits 200A and 200E in series to a vapor compression heat pump 405,in accordance with another embodiment of the present disclosure. FIG. 5is a schematic diagram of a cogeneration system including a vaporcompression heat pump coupled via conduits 200A and 200E in series to aBrayton-cycle heat operatively, in accordance with another embodiment ofthe present disclosure. In some applications, the cogeneration system 15can be configured to move heat transfer fluid from heat pump 405 to theheat engine 105 (or vice versa) rather than separately to eachcomponent, as previously shown in FIG. 2, where the conduits 200 are inconfigured in a parallel configuration.

There are some advantages to moving the heating transfer fluid throughconduits 200 configured in series. For instance, a series configurationis less complex than a parallel conduit configuration because theplumbing system includes fewer components (e.g., fewer conduit sectionsand valves). In addition, the series configuration can use lesssophisticated components, such as pumps or valves, which are easier tooperate and configure. In an example embodiment shown in FIG. 4, theheat transfer fluid leaving the valve arrangement 510 can move alongconduit 200 (as indicated by the arrows) and through the condenser 430to absorb thermal energy from the working fluid of the heat pump 405.The heat transfer fluid can then continue moving to heat exchanger 140of heat engine 105 along conduit 200E. At the heat exchanger 140, theheat transfer fluid can absorb thermal energy from the working fluid ofthe heat engine 105. Upon receiving the thermal energy from heat engine105, the heat transfer fluid can move back to the valve arrangement 510via conduit 200A at which it can be distributed to other components ofthe cogeneration system. In some other embodiments, the cogenerationsystem 15 is constructed and arranged to move the heat transfer fluid ina direction opposite of that shown in FIG. 4. For example, asillustrated by FIG. 5, the heat transfer fluid can move from the heatengine 105 to the heat pump 405 (as indicated by the arrows) so that itcan absorb thermal energy prior to being distributed to other systemcomponents. Numerous other cogeneration system configurations will beapparent in light of the present disclosure.

Example System Operation Applications

The cogeneration systems of the present disclosure can be operated toprovide one or more services to the enclosure 500. Services, such asspace heating and/or cooling, water heating, and thermal and electricalenergy generation, can be supplied or otherwise provided to theenclosure 500 by operation of a heat engine, heat pump or combinationthereof. In an example embodiment, the cogeneration system 15 can beconfigured to determine whether to operate the heat engine 105 or heatpump 405 (or both) based on a number of factors. Factors, such asavailability of electricity from an energy supplier, market price ofelectricity and fuels (e.g., fossil or renewable chemical fuels),temperature of the surrounding environment, backup energy supplies(e.g., from the thermal or electrical energy storage systems), orservice demands of the enclosure 500 can be considered individually orcollectively to determine a manner in which to operate cogenerationsystem components.

FIG. 6 is a schematic diagram of a cogeneration system 15 configured tosupply space heating to the enclosure 500, in accordance with anembodiment of the present disclosure. As previously described herein,the heat engine 105 can generate both thermal and electrical energy. Inthis application, the cogeneration system 15 can operate the heat engine105 (as indicated by the shaded lines) to supply or otherwise provideheating to the enclosure 500 via the heat transfer fluid. The operationof the heat engine 105, as can be seen, is accomplished withoutoperating the heat pump 405. There are a number of instances in whichoperating only the heat engine 105 to generate thermal energy may bepreferred. In one such instance, the heat (co)generated by the heatengine in meeting the electric located is sufficient to satisfy the heatload. Other instances may include grid-connected situations when thesystem might generate electricity which can be exported to the gridwhile cogenerating at least sufficient heat to meet the heat load. As aresult, the cogeneration system 15 can be configured to operate the heatengine 105 (as indicated by shading and arrows) by itself when it ismost practical to do so. In the application shown in FIG. 6, the heattransfer fluid moves through the heat exchanger 140 to absorb thermalenergy from the working fluid of the heat engine 105. As can be seen,the high-temperature heat transfer fluid (as indicated by solid shading)moves from the heat engine 105 to the valve arrangement 510 via conduit200A (i.e. first conduit) attached to the heat engine 105. At the valvearrangement 510, the high-temperature heat transfer fluid can bedirected to a number of cogeneration system components. In thisinstance, the valve arrangement 510 directs the high-temperature heattransfer fluid to the inside heat exchanger 520A via conduit 200B. Onceat the heat exchanger 520A, ambient air of the enclosure 500 absorbsthermal energy from the heat transfer fluid, as previously describedherein, to heat the enclosure 500. Upon exiting the heat exchanger 520A,the heat transfer fluid is at a reduced temperature (as indicated byshading with zig-zag lines). The reduced-temperature heat transfer fluidmoves or otherwise flows back to the valve arrangement 510 and to theheat exchanger 140 via conduits 200C to repeat the heating cycle. As canbe seen, in addition to thermal energy, the heat engine 105 alsogenerates electricity (as indicated by heavy solid black lines) byoperating generator 170. This electricity can be supplied to any numberof cogeneration system components. In this instance, electricity istransmitted via electrical cables 300 to the control panel 570,electrical energy storage system 580, and power panel 540. In otherinstances, the generated electricity can be provided to one or moreenergy suppliers via an electrical connection with the grid.

FIG. 7 is a schematic diagram of a cogeneration system 15 configured tosupply water heating to the enclosure 500 using a heat engine 105, inaccordance with an embodiment of the present disclosure. As can be seen,the cogeneration system 15 can operate the heat engine 105 (as indicatedby shading and arrows) without operating the heat pump 405 to supply orotherwise provide water heating to the enclosure 500. Generallyspeaking, water heating can be for various purposes, such as domestichot water usage or hot water storage. As previously described, the heattransfer fluid can absorb thermal energy from heat exchanger 140 and itmoves towards the valve arrangement 510 via conduit 200A (firstconduit). At the valve arrangement 510, the high-temperature heattransfer fluid (as indicated by solid shading) can be directed to thethermal storage system 530 (e.g., a water heat tank) via conduit 200D.Once at the thermal energy storage system 530, fluid disposed in thestorage system 530 absorbs thermal energy from the high-temperature heattransfer fluid, for example via a heat exchanger disposed in a tank. Asa result, the temperature of fluid in the thermal storage system 530increases, and thus storing thermal energy therein. This stored thermalenergy can be maintained for a period of time (e.g., for weeks ormonths) with little or no further thermal inputs. Once stored in thermalstorage system 530, this thermal energy can be used to supply energy toother cogeneration system components, as will be described furtherherein. Upon exiting the thermal storage system 530, the heat transferfluid is at a reduced temperature (as indicated by shading with zig-zaglines). The reduced-temperature heat transfer fluid can move orotherwise flow back to the valve arrangement 510 and the heat exchanger140 via conduits 200C to repeat the heating cycle. As can be seen, theheat engine 105 also generates electricity which can be used to operatecogeneration system components or can be sold to energy suppliers, aspreviously described herein.

FIG. 8 is a schematic diagram of a cogeneration system 15 configured tosupply space heating and water heating to the enclosure 500 using a heatengine 105, in accordance with an embodiment of the present disclosure.As can be seen, the cogeneration system 15 can operate only the heatengine 105 (as indicated by shading and arrows) to provide both spaceand water heating to the enclosure 500. In this embodiment, for in thisinstance, the high-temperature heat transfer fluid (as indicated bysolid shading) can move from the heat exchanger 140 of the heat engine105 to the valve arrangement 510 via conduit 200A (first conduit). Atthe valve arrangement 510, the high-temperature heat transfer fluid canbe directed to heat exchanger 520A via conduit 200B and the thermalstorage system 530 (e.g., a water heat tank) via conduit 200D, aspreviously described herein. In an example embodiment, the valvearrangement 510 can simultaneously direct high-temperature heat transferfluid to both heat exchanger 520A and thermal storage system 530,thereby heating the enclosure 500 and storing thermal energy at the sametime. In other embodiments, the valve arrangement 510 may direct thehigh-temperature heat transfer fluid to one component first and then toanother. For instance, in one embodiment, the cogenerations system 15can be configured to prioritize demands for space heating ahead ofstoring thermal energy. In such an instance, the valve arrangement 510may direct all the high-temperature heat transfer fluid to heatexchanger 520A until a desired temperature within the enclosure 500 isachieved (e.g., 20° Celsius (C)). In other instances, the valvearrangement 510 may vary the amount of high-temperature heat transferfluid to each component (e.g., 75% to heat exchanger 520A and 25% tothermal storage system 530). Such an instance, may be desired when thethermal storage system requires only a limited input (e.g., when thetemperature of the fluid of the storage system is nearly the same as theheat transfer fluid). No matter its particular sequence or manner ofoperation, the cogeneration system 15 can use the heat engine 105 toboth heat the enclosure 500 and store thermal energy for subsequent useby the system 15, as previously described herein. Upon exiting the heatexchanger 520A and thermal storage system 530, the heat transfer fluidis at a reduced temperature (as indicated by shading with zig-zaglines). The reduced-temperature heat transfer fluid can return to thevalve arrangement 510 via conduits 200C to repeat the space heating andthermal energy storing cycles. As can be seen, the heat engine 105 alsogenerates electricity which can be used to operate cogeneration systemcomponents or can be sold to energy buyers over the grid, as previouslydescribed herein.

FIG. 9 is a schematic diagram of a cogeneration system configured tosupply electricity to the enclosure 500 using a heat engine 105, inaccordance with an embodiment of the present disclosure. In this exampleapplication, only the heat engine 105 is operated (as indicated byshading and arrows) for purposes of generating electricity because theheat pump 405 does not produce electricity. Rather, heat pumps, such asheat pump 405, consume electricity to produce heating and cooling, aswill be described further herein. The cogeneration system 15 can operatein this manner in a number of instances. For example, in one instance,the enclosure 500 may be demanding electricity, but not heating orcooling. As a result, the cogeneration system 15 can be configured tooperate just the heat engine 105 because there are no unfulfilled orunsatisfied thermal energy needs for the enclosure 500 (e.g., no heatingor cooling demands and thermal storage systems are at or nearly at fullcapacity). In other instances, the cogeneration system 15 can beconfigured to determine the most cost effective manner in which tosupply electricity. For example, if the demand for electricity occurswhen market prices for electricity are high (e.g., peak hours, such asearly morning hours) then the cogeneration system 15 may operate theheat engine 105 to produce electricity rather than purchasing it fromthe grid. As can be seen, in this instance, high-temperature heattransfer fluid (as indicated by solid shading) can move or otherwiseflow from the heat exchanger 140 to the valve arrangement 510 viaconduit 200A. From valve arrangement 510, the high-temperature heattransfer fluid can move to the outside heat exchanger 460 via conduit200E. Once at the heat exchanger 460, ambient air of the surroundingenvironment absorbs the thermal energy from the heat transfer fluidthereby allowing the cogeneration system 15 to dispose of thermal energythat is not needed to operate the system. Upon exiting the heatexchanger 460, the heat transfer fluid is at a reduced temperature (asindicated by shading with zig-zag lines). The reduced-temperature heattransfer fluid can move or otherwise flow back to the valve arrangement510 via conduits 200C to repeat the cycle to cool the heat engine 105.The electricity generated by the heat engine 105 can be used to operatecogeneration system components or can be sold to energy suppliers, aspreviously described herein.

FIG. 10 is a schematic diagram of a cogeneration system 15 configured tosupply space heating to the enclosure 500 using a heat pump 405, inaccordance with an embodiment of the present disclosure. As can be seen,the cogeneration system 15 can operate only the heat pump 405 (asindicated by shading and arrows) to heat to the enclosure 500. There area number of instances in which operating only the heat pump 405 togenerate thermal energy may be preferred. In one such instance, cost tooperate the heat engine 105 (e.g., price of fuel) may make operation ofthe engine 105 more expensive than purchasing electricity from an energysupplier. In some other instances, heating demands for the enclosure maybe high while its electricity demands are low (e.g., during late eveningand early morning hours when there is little to no activity happening inthe enclosure 500). Other instances may include situations when gridelectricity is available for relatively low prices or when there issurplus electricity available from on-site solar. As a result, thecogeneration system 15 can be configured to operate the heat pump 405 byitself using electricity from the grid when it is most practical to doso. In the application shown in FIG. 10, the heat transfer fluid movesthrough the condenser 430 of the heat pump 405 to absorb thermal energyfrom the working fluid of the heat pump 405. As can be seen, thehigh-temperature heat transfer fluid (as indicated by solid shading)moves from the heat pump 405 to the valve arrangement 510 via conduits200E and 200A. From the valve arrangement 510, the high-temperature heattransfer fluid can move to the inside heat exchanger 520A via conduit200B. Once at the heat exchanger 520A, ambient air of the enclosure 500absorbs thermal energy from the heat transfer fluid, as previouslydescribed herein, to heat the enclosure 500. Upon exiting the heatexchanger 520A, the heat transfer fluid is at a reduced temperature (asindicated by shading with zig-zag lines). The reduced-temperature heattransfer fluid can move back to the condenser 430 via conduits 200C torepeat the heating cycle.

While the heat transfer fluid in conduit 200E absorbs thermal energyfrom the working fluid of the heat pump 405, the working fluid is alsoabsorbing thermal energy from heat transfer fluid in conduit 200F. Ascan be seen, upon moving through the reducing valve 440, the temperatureof the working fluid has been reduced. To increase its temperature andthus ready the working fluid to enter the compressor 420, the workingfluid can move through an evaporator 450. At the evaporator 450, thelow-temperature working fluid absorbs thermal energy fromhigher-temperature heat transfer fluid thereby raising the temperatureof the working fluid. In addition, the temperature of the heat transferfluid in conduit 200F is reduced. After exiting the evaporator 450, thelow-temperature heat transfer fluid (as indicated by lightly dottedshading) can move from the heat pump 405 to the valve arrangement 510via conduit 200H. From the valve arrangement 510, the low-temperatureheat transfer fluid can move to the outside heat exchanger 460 viaconduit 200G. Once at heat exchanger 460, the heat transfer fluidabsorbs thermal energy from ambient air of the surrounding to increasethe temperature of the fluid. Upon exiting the heat exchanger 460, theheat transfer fluid is at an increased temperature (as indicated by moreheavily dotted shading). The increased-temperature heat transfer fluidmoves back to the evaporator 450 via conduits 200F to repeat the cycle.

FIG. 11 is a schematic diagram of a cogeneration system 15 configured tosupply water heating to the enclosure 500 using a heat pump 405, inaccordance with an embodiment of the present disclosure. In an exampleapplication, the cogeneration system 15 can operate only the heat pump405 (as indicated by shading and arrows) to provide water heating to theenclosure 500. In the application shown in FIG. 11, the heat transferfluid absorbs thermal energy from the working fluid via the condenser430 of the heat pump 405. As can be seen, the high-temperature heattransfer fluid (as indicated by solid shading) moves from the heat pump405 to the valve arrangement 510 via conduits 200E and 200A. From thevalve arrangement, the high-temperature heat transfer fluid moves to thethermal storage system 530 (e.g., a water heat tank) via conduit 200D.Once at the thermal storage system 530, the fluid disposed in thestorage system 530 absorbs thermal energy from the high-temperature heattransfer fluid, for example via a heat exchanger disposed in a tank, aspreviously described herein. Upon exiting the thermal storage system530, the heat transfer fluid is at a reduced temperature (as indicatedby shading with zig-zag lines). The reduced-temperature heat transferfluid can move back to the condenser 430 of the heat pump 405 viaconduits 200C to repeat the water heating cycle. Also shown is a conduit200F attached to the evaporator 450 and configured to supplylow-temperature heat transfer fluid to cogeneration system components tooperate the heat pump 405, as previously described above in relation toFIG. 10.

FIG. 12 is a schematic diagram of a cogeneration system 15 configured tosupply space heating and water heating to the enclosure 500 using a heatpump 405, in accordance with an embodiment of the present disclosure. Ascan be seen, the cogeneration system 15 can operate the heat pump 405(as indicated by shading and arrows) without operating the heat engine105 (as indicated by no shading and arrows) to provide both spaceheating and water heating to the enclosure 500. As can be seen, in thisinstance, high-temperature heat transfer fluid (as indicated by solidshading) moves from the condenser 430 to the valve arrangement 510 viaconduits 200E and 200A. From the valve arrangement 510, high-temperatureheat transfer fluid moves to heat exchanger 520A via conduit 200B andthe thermal storage system 530 (e.g., a water heat tank) via conduit200D. The heat pump 405 can supply space and water heating in a numberof fashions, such as simultaneously, individually (e.g., supplying onecomponent than another), or proportionally (75% of heat transfer fluidto one component and 25% to another) as previously described herein.Upon exiting the heat exchanger 520A and thermal storage system 530, theheat transfer fluid is at a reduced temperature (as indicated by shadingwith zig-zag lines). The reduced-temperature heat transfer fluid movesback to the condenser 430 via conduits 200C to repeat the space andwater heating cycle. Also shown is conduit 200F that supplieslow-temperature heat transfer fluid to cogeneration system components tooperate the heat pump 405, as previously described above in relation toFIGS. 10 and 11.

FIG. 13 is a schematic diagram of a cogeneration system 15 configured tosupply space cooling to the enclosure 500 using a heat pump 405, inaccordance with an embodiment of the present disclosure. As previouslydescribed herein, the heat pump 405 can also provide space cooling tothe enclosure 500. In this application, the cogeneration system 15 canoperate the heat pump 405 (as indicated by shading and arrows) to supplyor otherwise provide space cooling to the enclosure 500 via the heattransfer fluid. Note that the enclosure 500 can be cooled by the heatpump 405 without operating the heat engine 105 for reasons providedabove. As a result, the cogeneration system 15 can be configured tooperate the heat pump 405 by itself using electricity from the grid whenit is most practical to do so. In the application shown in FIG. 13, theworking fluid of the heat pump 405 absorbs thermal energy from the heattransfer fluid flowing through the evaporator 450. As a result, thetemperature of the heat transfer fluid is reduced (as indicated bylighting dotted shading). Upon exiting the evaporator 450, thelow-temperature heat transfer fluid can move or otherwise flow from theheat pump 405 to the valve arrangement 510 via conduit 200F. From thevalve arrangement 510, the low-temperature heat transfer fluid can moveto the inside heat exchanger 520B via conduit 200I. Once at heatexchanger 520B, the heat transfer fluid absorbs thermal energy fromambient air of the enclosure 500 and thereby cooling the enclosure 500.Upon exiting the heat exchanger 520B, the heat transfer fluid is at anincreased temperature (as indicated by more heavily dotted shading). Theincreased-temperature heat transfer fluid moves back to the evaporator450 via conduits 200H to repeat the cooling cycle.

While the working fluid is absorbing thermal energy from heat transferfluid in conduit 200F to supply cooling to the enclosure, heat transferfluid in conduit 200E absorbs thermal energy from the working fluid ofthe heat pump 405. As can be seen, in this instance, high-temperatureheat transfer fluid (as indicated by solid shading) moves from thecondenser 430 to the valve arrangement 510 via conduits 200E and 200A.From the valve arrangement 510, the high-temperature heat transfer fluidcan move to the outside heat exchanger 460 via conduit 200G. Once at theheat exchanger 460, ambient air of the surrounding environment absorbsthe thermal energy from the heat transfer fluid thereby allowing thecogeneration system 15 to dispose of thermal energy that is not neededto operate the system. Upon exiting the heat exchanger 460, the heattransfer fluid is at a reduced temperature (as indicated by shading withzig-zag lines). The reduced-temperature heat transfer fluid can moveback to the condenser 430 via conduits 200H to repeat the cycle todispose of thermal energy generated by the heat pump 405.

FIG. 14 is a schematic diagram of a cogeneration system 15 configured tosupply water heating and space cooling to the enclosure 500 using a heatpump 405, in accordance with an embodiment of the present disclosure.Rather than transferring the thermal energy generated by the heat pump405 during the cooling cycle to the environment as shown in FIG. 13, thecogeneration system 15 can be configured to recovery this energy in anumber of ways. For instance, in one illustrative embodiment, thecogeneration system 15 can recover or otherwise capture thermal energygenerated by the heat pump 405 and store it for later use. As can beseen, the heat pump 405 can absorb thermal energy from the heat transferfluid moving through the third conduit 200F to cool the enclosure 500,as previous described in relation to FIG. 13. In addition, thecogeneration system 15 can store the thermal energy generated by theheat pump 405 as it provides space cooling to the enclosure 500. Asshown, the high-temperature heat transfer fluid (as indicated by solidshading) moves from the condenser 430 to the valve arrangement 510 viaconduits 200E and 200A. From the valve arrangement 510, thehigh-temperature heat transfer fluid can move to thermal storage system530 (e.g., a water heat tank) via conduit 200D. Once at the thermalstorage system 530, fluid disposed in the storage system 530 absorbsthermal energy from the high-temperature heat transfer fluid, forexample via a heat exchanger disposed in a tank, as previously describedherein. Upon exiting the thermal storage system 530, the heat transferfluid is at a reduced temperature (as indicated by shading with zig-zaglines). The reduced-temperature heat transfer fluid can move back to thecondenser 430 via conduits 200C to repeat the thermal storage cycle.Note that, in some embodiments, thermal energy can be stored by thecogeneration system 15 while it simultaneously supplies cooling to theenclosure 500. While in other embodiments, the cogeneration system 15can supply cooling to the enclosure 500 and intermittently orperiodically store thermal energy as needed (e.g., maintain a thresholdlevel or capacity). For example, the valve arrangement 510 can initiallydirect high-temperature heat transfer fluid to the thermal storagesystem 530 and then to the outside heat exchanger 460 once the system530 is a desired thermal energy level. Thus, the thermal storage system,in some embodiments, can periodically receive thermal energy to maintainan amount of thermal energy stored in the thermal storage system above athreshold level. A threshold level can be a minimum amount of energythat can be stored in the thermal storage system 539 to operate thecogeneration system 15 for a period of time (e.g., 6 hours, 12, hours, aday or several days). Numerous thermal storage configurations will beapparent in light of the present disclosure.

FIG. 15 is a schematic diagram of a cogeneration system 15 configured tode-ice a heat reservoir, such as an outside heat exchanger 460 using aheat pump 405, in accordance with an embodiment of the presentdisclosure. Under some conditions (e.g., cold days in which the heatpump operates at a high coefficient of performance) ice may form on theoutside heat exchanger 460 and thereby preventing the heat exchanger 460from functioning properly. Previous systems require that unwantedcooling be supplied to the enclosure 500 and/or physical changes tocomponents be made (e.g., adding or swapping out valves) to remove orotherwise de-ice the heat exchanger. This unwanted cooling can beunpleasing or otherwise cause discomfort to individuals in the enclosure(e.g., cooling the enclosure during the winter). In addition, physicallychanging or adding components to the system is time consuming, and thusit is inconvenient and often times causes delays with system operation.The cogenerations systems of the present disclosure are not so limited.In one illustrative embodiment, the cogeneration system 15 can beconfigured to prevent an accumulation of excess ice or otherwise de-icethe outside heat exchanger 460 without cooling the enclosure 500 orchanging components. In an example application, the heat pump 405 can beoperated by itself (i.e., without the heat engine 105) to heat theoutside heat exchanger 460, and thus prevent an accumulation of ice ormelt ice present on the heat exchanger. In such an application, thethermal storage system 530 can provide thermal energy to operate theheat pump 405 instead of the outside heat exchanger 460. In more detail,as illustrated in FIG. 15, the working fluid of the heat pump 405absorbs thermal energy from the heat transfer fluid moving through theevaporator 450, as previously described herein. As a result, thetemperature of the heat transfer fluid is reduced (as indicated bylightly dotted shading). Upon exiting the evaporator 450, thelow-temperature heat transfer fluid can move from the heat pump 405valve arrangement 510 via conduit 200F. From the valve arrangement 510,the low-temperature heat transfer fluid can move to the thermal storagesystem 530 via conduit 200K. Once at storage system 530, the heattransfer fluid absorbs thermal energy from fluid therein. Upon exitingthe thermal storage system 530, the heat transfer fluid is at anincreased temperature (as indicated by more heavily dotted shading). Theincreased-temperature heat transfer fluid moves back to the evaporator450 via conduits 200H to operate the heat pump 405.

While the working fluid is also absorbing thermal energy from heattransfer fluid in conduit 200F, the heat transfer fluid in conduit 200Eabsorbs thermal energy from the working fluid of the heat pump 405 toraise its temperature. The high-temperature heat transfer fluid can thenbe supplied to the outside heat exchanger 460 to heat or otherwisede-ice the heat exchanger 460. In more detail, as illustrated in theembodiment of FIG. 15, high-temperature heat transfer fluid (asindicated by solid shading) moves from the condenser 430 to the valvearrangement 510 via conduits 200E and 200A. From the valve arrangement510, the high-temperature heat transfer fluid can move to the outsideheat exchanger 460 via conduit 200G. Once at the heat exchanger 460,ambient air of the surrounding environment absorbs the thermal energyfrom the heat transfer fluid thereby causing the ice formed on the heatexchanger to melt. Upon exiting the heat exchanger 460, the heattransfer fluid is at a reduced temperature (as indicated by shading withzig-zag lines) and moves to the condenser 430 via conduits 200H torepeat the de-icing cycle.

FIG. 16 is a schematic diagram of a cogeneration system 15 configured tosupply space heating to the enclosure 500 using a heat pump 405 and athermal storage system 530, in accordance with an embodiment of thepresent disclosure. The cogeneration system 15, in some embodiments, canbe configured to use the thermal storage system 530 as high-temperaturereservoir rather than utilizing the outside heat exchanger 460. Such aconfiguration may be preferable as the temperature of the ambient air ofthe surrounding environment decreases. This is particularly the case,when the temperature of the surrounding environment is approximately thesame as the heat transfer fluid so that there is little or no thermalenergy transferred from one to the other. To avoid such situations, thecogeneration system 15 can utilize the stored energy of the thermalstorage system 530 as a heat source to operate the heat pump 405. Aspreviously described above, the working fluid of the heat pump 405absorbs thermal energy from the heat transfer fluid moving through theevaporator 450, as previously described herein. As a result, thetemperature of the heat transfer fluid is reduced (as indicated bylightly dotted shading). Upon exiting the evaporator 450, thelow-temperature heat transfer fluid can move from the heat pump 405 tothe valve arrangement 510 via conduit 200F. From the valve arrangement510, the low-temperature heat transfer fluid can move to the thermalstorage system 530 via conduit 200K. Once at storage system 530, theheat transfer fluid absorbs thermal energy from fluid therein. Uponexiting the thermal storage system 530, the heat transfer fluid is at anincreased temperature (as indicated by more heavily dotted shading). Theincreased-temperature heat transfer fluid moves back to the evaporator450 via conduits 200H to operate the heat pump 405. In addition, theheat transfer fluid in conduit 200E absorbs thermal energy from theworking fluid of the heat pump 405 and is transmitted to the inside heatexchanger 520A to heat the enclosure, as previously described herein.

FIG. 17 is a schematic diagram of a cogeneration system 15 configured tosupply space heating to the enclosure 500 using a heat pump 405, a heatengine 105 and a heat reservoir (an outside heat exchanger 460), inaccordance with an embodiment of the present disclosure.

FIG. 18 is a schematic diagram of a cogeneration system 15 configured tosupply water heating to the enclosure 500 using a heat pump 405 and aheat engine 105, in accordance with an embodiment of the presentdisclosure.

FIG. 19 is a schematic diagram of a cogeneration system 15 configured tosupply space and water heating to the enclosure 500 using a heat pump405 and a heat engine 105, in accordance with an embodiment of thepresent disclosure.

As shown in FIGS. 17-19, the cogeneration system 15, in some instances,can operate both the heat engine 105 and heat pump 405 to heat theenclosure 500. There are number situations in which the cogenerationsystem may operate both the heat engine 105 and heat pump 405. In onesuch situation, for example, the heating demands for the enclosure 500may exceed the thermal output of the heat engine 105 by itself. In othercases, it may be more cost effective to use electricity generated by theheat engine 105 rather than from the grid (e.g., at peak times of energyconsumption). Or in yet other cases, electricity may not be availablefrom electrical energy suppliers via the grid (e.g., electrical supplierdisconnects enclosure from the grid or during a blackout).

In an example embodiment, as shown in FIGS. 17-19, the heat engine 105can produce both thermal and electrical energy, as previously describedherein. A portion of the electricity produced by the heat engine 105 canbe used to operate the heat pump. The remaining portion of theelectricity can be used to power electrical components of the enclosure500 (e.g., power panel 540 and control panel 570) or be stored byelectrical energy storage system 580 for future use. As can be seen, theheat transfer fluids within conduits 200A (i.e. first conduit) and 200E(i.e. second conduit) each absorb thermal energy from the working fluidsof the heat engine 105 and heat pump 405 (respectively). As discussedabove and as shown in FIGS. 3 and 4, the high-temperature heat transferfluids can be combined in series or parallel fashion so that the fluidis moved to the inside heat exchanger 520A to heat the enclosure 500. Inaddition, the working fluid of the heat pump 405 can also absorb thermalenergy from the heat transfer fluid in the conduit 200F (i.e. thirdconduit) in communication with other cogeneration system components(e.g., the outside heat exchanger 460 or thermal storage system 530) tooperate the heat pump 405, as previously described herein. In some otherapplications, the combined high-temperature heat transfer fluid can alsobe supplied to the thermal storage system 530, as shown in FIG. 18, tostore thermal energy. In yet other applications, the cogeneration system15 may move the combined high-temperature heat transfer fluid to boththe inside heat exchanger 520A and thermal storage system 530 toaccomplish both space heating of the enclosure 500 and water heating, asshown in FIG. 19. As previously described herein, the cogenerationsystem 15 can be configured to perform both space heating and waterheating operations simultaneously or one at a time. In some such cases,water heating may occur only periodically while space heating isperformed. Numerous other cogeneration system applications will beapparent in light of the present disclosure.

FIG. 20 is a schematic diagram of a cogeneration system 15 configured tosupply space cooling to the enclosure using a heat pump 405 and a heatengine 105, in accordance with an embodiment of the present disclosure.

FIG. 21 is a schematic diagram of a cogeneration system 15 configured tosupply water heating and space cooling to the enclosure using a heatpump 405 and a heat engine 105, in accordance with an embodiment of thepresent disclosure.

As shown in the embodiments illustrated in FIGS. 20 and 21, thecogeneration system 15 can operate both the heat engine 105 and heatpump 405 to cool the enclosure 500, as previously described above. In anexample embodiment, as shown, the heat engine 105 can produce boththermal and electrical energy, as previously described herein. Some ofthe electricity from the heat engine 105 can be used to operate the heatpump 405 to supply cooling to the enclosure 500. As can be seen, theheat transfer fluids within conduits 200A (first conduit) and 200E(second conduit) each absorb thermal energy from the working fluids ofthe heat engine 105 and heat pump 405 (respectively). Thehigh-temperature heat transfer fluids can be combined to transferunwanted thermal energy from the heat engine 105 and heat pump 405 to anoutside heat exchanger 460 at which the energy can be absorbed into theenvironment, as previously described herein. In some other applications,the combined high-temperature heat transfer fluid can also be suppliedto the thermal storage system 530, as shown in FIG. 21, to store thermalenergy produced by the heat engine 105 and heat pump 405 for subsequentuse by the cogeneration system components. In addition, the workingfluid of the heat pump 405 can also absorb thermal energy from the heattransfer fluid in conduit 200F (third conduit) in communication withother cogeneration system components (e.g., the inside heat exchanger520B) to supply cooling to the enclosure 500, as previously describedherein.

FIG. 22 is a schematic diagram of a cogeneration system 15 configured tode-ice a heat reservoir such as an outside heat exchanger 460 using aheat pump 405 and a heat engine 105, in accordance with an embodiment ofthe present disclosure.

FIG. 23 is a schematic diagram of a cogeneration system 15 configured tosupply space heating to the enclosure 500 using a heat pump 405, heatengine 105, and a thermal storage system 530, in accordance with anembodiment of the present disclosure.

As shown in the embodiments illustrated in FIGS. 22 and 23, thecogeneration system 15 may be configured to utilize the thermal storagesystem 530 as a high-temperature reservoir instead of the outside heatexchanger 460. This is particularly the case when the outside heatexchanger 460 forms ice thereon or the air temperature of theenvironment is so low as to adversely affect the performance of the heatpump 405. In an example application, the heat pump 405 can receivethermal energy from the thermal storage system 530 via the heat transferfluid in conduit 200F. As can be seen, the thermal energy produced bythe heat engine 105 and heat pump 405 can be transferred to the outsideheat exchanger 460 via high-temperature heat transfer fluid withinconduits 200A and 200E. Once received, the high-temperature heattransfer fluid can transfer thermal energy to the outside heat exchanger460 and thereby causing the ice formed thereon to melt. Similarly, thecogeneration system 15 can direct the high-temperature heat transferfluid to inside heat exchanger 520A to heat the enclosure 500, as shownin FIG. 23. Numerous other cogeneration system applications will beapparent in light of the present disclosure.

SUMMARY

One example embodiment of the present disclosure provides a cogenerationsystem for providing heating, cooling, and electricity to an enclosure,the cogeneration system including a heat engine configured for heatingand supplying electricity to the enclosure; a heat pump configured forheating and cooling of the enclosure; a first conduit coupled to theheat engine, wherein the first conduit is filled with a first heattransfer fluid, and the first conduit is constructed and arranged totransfer the first heat transfer fluid from the heat engine to theenclosure such that thermal energy is transferred from the first heattransfer fluid to the enclosure to provide heating to the enclosure; asecond conduit coupled to the heat pump, wherein the second conduit isfilled with the first heat transfer fluid, and the second conduit isconstructed and arranged to transfer the first heat transfer fluid fromthe heat pump to the enclosure such that thermal energy is transferredfrom the first heat transfer fluid to the enclosure to provide heatingto the enclosure; and a third conduit coupled to the heat pump, whereinthe third conduit is filled with a second heat transfer fluid, and thethird conduit is constructed and arranged to transfer the second heattransfer fluid from the heat pump to the enclosure such that thermalenergy is absorbed by the second heat transfer fluid from the enclosureto provide cooling to the enclosure; and wherein said heat pump isconfigured to supply heating and cooling to the enclosuresimultaneously.

Another example embodiment of the present disclosure provides acogeneration system for providing heating and electricity to anenclosure, the cogeneration system including a heat engine configuredfor heating and supplying electricity to the enclosure; a heat pumpconfigured for heating of the enclosure; a first conduit coupled to theheat engine, wherein said first conduit is filled with a heat transferfluid, and the first conduit is constructed and arranged to transfer theheat transfer fluid from the heat engine to the enclosure such thatthermal energy is transferred from the heat transfer fluid to theenclosure to provide heating to the enclosure; and a second conduitcoupled to the heat pump and the first conduit, wherein the secondconduit is filled with the heat transfer fluid, and said second conduitis constructed and arranged to transfer the heat transfer fluid from theheat pump to the enclosure such that thermal energy is transferred fromthe heat transfer fluid to the enclosure to provide heating to theenclosure; and wherein the first conduit and the second conduit arefluidly coupled such that the heat transfer fluid in the first conduitis the same as the heat transfer fluid in the second conduit.

Another example embodiment of the present disclosure provides acogeneration system for providing heating and electricity to anenclosure, the cogeneration system including a heat engine configured toproduce heating and electricity for the enclosure; a heat pumpconfigured to produce heating for the enclosure; a heat reservoirconstructed and arranged to transfer thermal energy from an area outsideof the enclosure to the heat pump; a thermal storage system associatedwith the enclosure and including a thermal storage system heatexchanger; a first conduit coupled to the heat engine, wherein the firstconduit is filled with a first heat transfer fluid, and the firstconduit is constructed and arranged to transfer the first heat transferfluid from the heat engine to the thermal storage system heat exchangersuch that thermal energy is transferred from the first heat transferfluid to the thermal storage system; and a second conduit coupled to theheat pump, wherein the second conduit is filled with the first heattransfer fluid, and the second conduit is constructed and arranged totransfer the first heat transfer fluid from the heat pump to the thermalstorage system heat exchanger such that thermal energy is transferredfrom the first heat transfer fluid to the thermal storage system; andwherein the first conduit and the second conduit are fluidly coupled tothe thermal storage system heat exchanger such that the first heattransfer fluid from the first conduit and the second conduit istransferred to the thermal storage system heat exchanger to storethermal energy within the thermal storage system.

Another example embodiment of the present disclosure provides acogeneration system for providing heating, cooling and electricity to anenclosure, the cogeneration system including a heat engine configured toproduce heating and electricity for the enclosure; a heat pumpconfigured to produce heating and cooling for the enclosure; a firstconduit coupled to the heat engine, wherein the first conduit is filledwith a first heat transfer fluid, and the first conduit is constructedand arranged to transfer the first heat transfer fluid from the heatengine to the enclosure such that thermal energy is transferred from thefirst heat transfer fluid to the enclosure to provide heating to theenclosure; a second conduit coupled to the heat pump, wherein the secondconduit is filled with the first heat transfer fluid, and the secondconduit is constructed and arranged to transfer the first heat transferfluid from the heat pump to the enclosure such that thermal energy istransferred from the first heat transfer fluid to the enclosure toprovide heating to the enclosure; a third conduit coupled to the heatpump, wherein said third conduit is filled with a second heat transferfluid, and the third conduit is constructed and arranged to transfer thesecond heat transfer fluid from the heat pump to the enclosure such thatthermal energy is absorbed by the second heat transfer fluid from theenclosure to provide cooling to the enclosure; and a valve arrangementconstructed and arranged to selectively couple the first conduit and thesecond conduit to transfer the first heat transfer fluid to theenclosure to provide at least one of space heating and water heating,and to selectively couple the third conduit to transfer the second heattransfer fluid to the enclosure to provide at least one of space coolingand a source of thermal energy for the heat pump.

Another example embodiment of the present disclosure provides acogeneration system for providing heating, cooling, and electricity toan enclosure, the cogeneration system including a heat engine configuredfor heating and supplying electricity to the enclosure; a heat pumpconfigured for heating and cooling of the enclosure; a first conduitcoupled to the heat engine, wherein the first conduit is filled with afirst heat transfer fluid, and the first conduit is constructed andarranged to transfer the first heat transfer fluid from the heat engineto the enclosure such that thermal energy is transferred from the firstheat transfer fluid to the enclosure to provide heating to theenclosure; a second conduit coupled to the heat pump, wherein the secondconduit is filled with the first heat transfer fluid, and the secondconduit is constructed and arranged to transfer the first heat transferfluid from the heat pump to the enclosure such that thermal energy istransferred from the first heat transfer fluid to the enclosure toprovide heating to the enclosure; and a third conduit coupled to saidheat pump, wherein said third conduit is filled with a second heattransfer fluid, and the third conduit is constructed and arranged totransfer the second heat transfer fluid from the heat pump to theenclosure such that thermal energy is absorbed by the second heattransfer fluid from the enclosure to provide cooling to the enclosure;and wherein the heat engine is configured to supply electricity tooperate the heat pump.

Another example embodiment of the present disclosure provides a methodof providing heating, cooling and electricity to an enclosure using acogeneration system, the method including generating thermal energy andelectricity by operation of a heat engine; providing thermal energy byoperation of a heat pump using the electricity from the heat engine;transferring thermal energy from the heat engine and the heat pump to afirst heat transfer fluid; providing at least one of space heating andwater heating to the enclosure via the first heat transfer fluid at aheating system heat exchanger constructed and arranged to be coupled toa heating system associated with the enclosure; and providing spacecooling to the enclosure by operation of the heat pump via a second heattransfer fluid that absorbs thermal energy from the enclosure at acooling system heat exchanger constructed and arranged to be coupled toa cooling system associated with the enclosure, wherein at least one ofspace heating and water heating are provided to the enclosuresimultaneously with space cooling to the enclosure.

Another example embodiment of the present disclosure provides a methodof providing heating, cooling and electricity to an enclosure using acogeneration system, the method including generating thermal energy andelectricity by operation of a heat engine; providing thermal energy byoperation of a heat pump; transferring thermal energy from the heatengine and the heat pump to a first heat transfer fluid; moving thefirst heat transfer fluid through a valve arrangement, the valvearrangement constructed and arranged to distribute the first heattransfer fluid to one or more cogeneration system components; providingat least one of space heating and water heating to the enclosure via thefirst heat transfer fluid at a heating system heat exchanger constructedand arranged to be coupled to a heating system associated with theenclosure; moving a second heat transfer fluid through the valvearrangement, the valve arrangement constructed and arranged todistribute the second heat transfer fluid to one or more cogenerationsystem components without the first heat transfer fluid contacting thesecond heat transfer fluid; and providing space cooling to the enclosureby operation of the heat pump via the second heat transfer fluid thatabsorbs thermal energy from the enclosure at a cooling system heatexchanger constructed and arranged to be coupled to a cooling systemassociated with the enclosure.

Another example embodiment of the present disclosure provides a methodof providing heating, cooling and electricity to an enclosure using acogeneration system, the method including generating thermal energy andelectricity by operation of a heat engine; providing thermal energy byoperation of a heat pump; transferring thermal energy from the heatengine and the heat pump to a first heat transfer fluid; providing atleast one of space heating and water heating to the enclosure via thefirst heat transfer fluid at a heating system heat exchanger constructedand arranged to be coupled to a heating system associated with theenclosure; and providing thermal energy to a thermal storage system heatexchanger via at least one of the first heat transfer fluid and a secondheat transfer fluid, the thermal storage system heat exchangerconstructed and arranged to be coupled to a thermal storage systemassociated with the enclosure.

Yet another example embodiment of the present disclosure provides acogeneration system including a heat engine and a heat pump which may beconfigured to provide only heating (for example for space heating, waterheating, and/or process heating) but no electric output. Unlike thestate of the art in other engine-driven heat pumps, this cogenerationsystem may go through the intermediate stage of producing electricity,100% of which would be used to drive the heat pump, thus no electricoutput.

The foregoing description of the embodiments of the present disclosurehas been presented for the purposes of illustration and description. Itis not intended to be exhaustive or to limit the present disclosure tothe precise form disclosed. Many modifications and variations arepossible in light of this disclosure. It is intended that the scope ofthe present disclosure be limited not by this detailed description, butrather by the claims appended hereto.

What is claimed is:
 1. A method of providing heating, cooling andelectricity to an enclosure using a cogeneration system, the methodcomprising: generating thermal energy and electricity by operation of aheat engine; providing thermal energy by operation of a heat pump usingthe electricity from the heat engine; transferring thermal energy fromthe heat engine and the heat pump to a first heat transfer fluid;providing at least one of space heating and water heating to theenclosure via the first heat transfer fluid at a heating system heatexchanger constructed and arranged to be coupled to a heating systemassociated with the enclosure; and providing space cooling to theenclosure by operation of the heat pump via a second heat transfer fluidthat absorbs thermal energy from the enclosure at a cooling system heatexchanger constructed and arranged to be coupled to a cooling systemassociated with the enclosure, wherein at least one of space heating andwater heating are provided to the enclosure simultaneously with spacecooling to the enclosure.
 2. The method of claim 1, further comprising:providing thermal energy to a thermal storage system heat exchanger, thethermal storage system heat exchanger constructed and arranged to becoupled to a thermal storage system associated with the enclosure. 3.The method of claim 2, wherein at least one of space heating and waterheating is provided to the enclosure before thermal energy is providedto the thermal storage system heat exchanger.
 4. The method of claim 2,wherein thermal energy is provided to the thermal storage systemperiodically to maintain an amount of thermal energy stored in thethermal storage system above a threshold level.
 5. The method of claim2, further comprising: providing thermal energy from the thermal storagesystem heat exchanger to the second heat transfer fluid; and providingthermal energy from the second heat transfer fluid to a heat reservoirto prevent excess ice from accumulating on the heat reservoir.
 6. Themethod of claim 2, further comprising: providing thermal energy from thethermal storage system heat exchanger to the second heat transfer fluid;and providing thermal energy to the heat pump by absorption of thermalenergy from the second heat transfer fluid to operate the heat pump. 7.The method of claim 2, further comprising providing electricity to anelectrical energy storage system, the electrical energy storage systemconstructed and arranged to selectively transfer the electricity to atleast one of the heat pump and a power panel.
 8. A method of providingheating, cooling and electricity to an enclosure using a cogenerationsystem, the method comprising: generating thermal energy and electricityby operation of a heat engine; providing thermal energy by operation ofa heat pump; transferring thermal energy from the heat engine and theheat pump to a first heat transfer fluid; moving the first heat transferfluid through a valve arrangement, the valve arrangement constructed andarranged to distribute the first heat transfer fluid to one or morecogeneration system components; providing at least one of space heatingand water heating to the enclosure via the first heat transfer fluid ata heating system heat exchanger constructed and arranged to be coupledto a heating system associated with the enclosure; moving a second heattransfer fluid through the valve arrangement, the valve arrangementconstructed and arranged to distribute the second heat transfer fluid toone or more cogeneration system components without the first heattransfer fluid contacting the second heat transfer fluid; and providingspace cooling to the enclosure by operation of the heat pump via thesecond heat transfer fluid that absorbs thermal energy from theenclosure at a cooling system heat exchanger constructed and arranged tobe coupled to a cooling system associated with the enclosure.
 9. Themethod of claim 8, further comprising: moving the first heat transferfluid from at least one of the heat engine and heat pump and through thevalve arrangement in a first direction to supply thermal energy to theheating system heat exchanger to provide heating to the enclosure; andmoving the first heat transfer fluid from the heating system heatexchanger and through the valve arrangement in a second directionopposite the first direction to return the first heat transfer fluid toat least one of the heat engine and the heat pump so that the first heattransfer fluid absorbs further thermal energy from at least one of theheat engine and the heat pump.
 10. The method of claim 8, furthercomprising: moving the second heat transfer fluid from the heat pump andthrough the valve arrangement in a first direction to receive thermalenergy from the cooling system heat exchanger to provide cooling to theenclosure; and moving the second heat transfer fluid from the coolingsystem heat exchanger and through the valve arrangement in a seconddirection opposite the first direction to return the second heattransfer fluid the heat pump at which further thermal energy istransferred from the second heat transfer fluid to the heat pump. 11.The method of claim 8, further comprising: moving the second heattransfer fluid from a thermal storage system heat exchanger and throughthe valve arrangement in a first direction to supply thermal energy tothe heat pump to operate the heat pump; and moving the second heattransfer fluid from the heat pump and through the valve arrangement in asecond direction opposite the first direction to return the second heattransfer fluid to the thermal storage system heat exchanger.
 12. Themethod of claim 8, further comprising: moving the second heat transferfluid from a thermal storage system heat exchanger and through the valvearrangement in a first direction to supply thermal energy to heatreservoir to prevent excess ice from accumulating on the heat reservoir;and moving the second heat transfer fluid from the heat reservoir andthrough the valve arrangement in a second direction opposite the firstdirection to return the second heat transfer fluid to the thermalstorage system heat exchanger.
 13. A method of providing heating,cooling and electricity to an enclosure using a cogeneration system, themethod comprising: generating thermal energy and electricity byoperation of a heat engine; providing thermal energy by operation of aheat pump; transferring thermal energy from the heat engine and the heatpump to a first heat transfer fluid; providing at least one of spaceheating and water heating to the enclosure via the first heat transferfluid at a heating system heat exchanger constructed and arranged to becoupled to a heating system associated with the enclosure; and providingthermal energy to a thermal storage system heat exchanger via at leastone of the first heat transfer fluid and a second heat transfer fluid,the thermal storage system heat exchanger constructed and arranged to becoupled to a thermal storage system associated with the enclosure. 14.The method of claim 13, further comprising providing space cooling tothe enclosure via the second heat transfer fluid that absorbs thermalenergy from the enclosure at a cooling system heat exchanger constructedand arranged to be coupled to a cooling system associated with theenclosure.
 15. The method of claim 13, further comprising supplyingelectricity generated by the heat engine to one or more energysuppliers.
 16. The method of claim 13, wherein thermal energy isprovided to the thermal storage system periodically to maintain anamount of thermal energy stored in the thermal storage system above athreshold level.